certification test report - raisus.rais.com/client_media/files/cad/0138ws017e - non-cbi... ·...

OMNI-Test Laboratories, Inc.

Non-Confidential Business Information

(Non-CBI)

Certification Test Report

RAIS A/S

Freestanding Wood Stove

Viva L Series Models: Viva 100 L (CA) USA, Viva 100 L G (CA) USA, Viva 100 L Classic (CA) USA, Viva

100 L G Classic (CA) USA, Viva 120 L (CA) USA, Viva 120 L G (CA) USA, Viva 120 L

Classic (CA) USA, Viva 120 L G Classic (CA) USA, Viva 160 L (CA) USA, Viva 160 L G

(CA) USA, Viva 160 L Classic (CA) USA, Viva 160 L G Classic (CA) USA

Prepared for: RAIS A/S

Industrivej 20, Vangen

DK-9900 Frederikshavn

Denmark

Prepared by: OMNI-Test Laboratories, Inc.

13327 NE Airport Way

Portland, OR 97230

(503) 643-3788

Test Period: 2/6/2017 - 2/13/2017

Report Date: April 2017

Report Number: 0138WS017E

All data and information contained in this report are confidential and proprietary to RAIS

A/S. Its significance is subject to the adequacy and representative character of the samples

and to the comprehensiveness of the tests, examinations, or surveys made. The contents of

this report cannot be copied or quoted, except in full, without specific, written authorization

from RAIS A/S and OMNI-Test Laboratories, Inc. No use of the OMNI-Test Laboratories,

Inc. name, logo, or registered mark (O-TL) is permitted, except as expressly authorized by

OMNI-Test Laboratories, Inc. in writing.

Model: Viva L Series

RAIS A/S Industrivej 20, Vangen


Denmark


AUTHORIZED SIGNATORIES

This report has been reviewed and approved by the following authorized signatories:

Technician:

__________________________

Aaron Kravitz


QA Review:

___________________________

Alex Tiegs, QA Administrator


Evaluation Decision:

__________________________

Sebastian Button, Testing Supervisor


______________

Issue Date

April 13, 2017

Model: Viva L Series RAIS A/S


DK-9900 Frederikshavn Denmark


TABLE OF CONTENTS

PREFACE ............................................................................................................... (3 pages)

1. SAMPLING PROCEDURES AND TEST RESULTS .......................................................4

Introduction ..........................................................................................................................5

Sampling Procedure .............................................................................................................5

Summary of Results .............................................................................................................5

Testing Narrative .................................................................................................................6

Summary Tables

Table 1 - Particulate Emissions Results ...............................................................................8

Table 2 - Particulate Emissions Results (First Hour)...........................................................8

Table 3 – B415.1 Efficiency and CO Emissions .................................................................9

Table 4 - Test Facility Conditions .......................................................................................9

Table 5 - Fuel Measurements and Crib Descriptions - Pretest ............................................9

Table 6 - Fuel Measurements and Crib Descriptions - Test ..............................................10

Table 7 - Dilution Tunnel Gas Measurements and Sampling Data ...................................10

Table 8 – Average Temperature Data ................................................................................10

Table 9 - Pretest Configurations ........................................................................................11

Table 10 - Test Configurations ..........................................................................................11

2. PHOTOGRAPHS/APPLIANCE DESCRIPTION ............................................................12

Fuel Photographs ...............................................................................................................13

Appliance Description .......................................................................................................18

3. TEST DATA BY RUN ......................................................................................................21

Run 1 ..................................................................................................................................24

Run 2 ..................................................................................................................................33

Run 3 ..................................................................................................................................42

Run 4 ..................................................................................................................................51

Run 5 ..................................................................................................................................60

Run 6 ..................................................................................................................................69

Run 7 ..................................................................................................................................78

Run 8 ..................................................................................................................................87

4. QUALITY ASSURANCE/QUALITY CONTROL ..........................................................96

Sample Analysis................................................................................................................ 98

Calibrations – EPA Method 28R, ASTM E2515, ASTM E2780 ....................................121

Example Calculations ......................................................................................................140

5. LABELING & OWNER’S MANUAL ............................................................................156

Appendix 1 Drawings – All Variants




Denmark

Section 1

Sampling Procedures and Test Results




INTRODUCTION

RAIS A/S retained OMNI to perform U.S. Environmental Protection Agency (EPA) certification

testing on the Viva L Series wood stove. The Viva L Series wood stove is a radiant-type room

heater. The firebox is constructed of mild steel. Usable firebox volume was measured to be 1.29

cubic feet and the stove is vented through a 6” flue collar located at the top of the unit.

The testing was performed at OMNI’s facilities in Portland, OR. The altitude of the laboratory is

30 feet above sea level. The unit was received in good condition and logged in on 1/30/2017,

then assigned and labeled with OMNI ID #2223. OMNI representatives Aaron Kravitz and

Sebastian Button conducted the certification testing and completed all testing by 2/13/2017.

This report is organized in accordance with the EPA-recommended outline and is summarized in

the Table of Contents immediately preceding this section. The results in this report are limited to

the item submitted.

SAMPLING PROCEDURE

The Viva L Series wood stove was tested in accordance with the U.S. EPA 40 CFR Part 60,

Subpart AAA – Standards of Performance for New Residential Wood Heaters using EPA

Method 28R, ASTM E2515 and ASTM E2780. Particulate emissions were measured using

sampling trains consisting of two filters (front and back).

The model Viva L Series was tested for thermal efficiency and carbon monoxide (CO) emissions

in accordance with CSA B415.1-10.

SUMMARY OF RESULTS

The weighted average emissions of the four test runs included in the results indicate a particulate

emission rate of 1.13 grams per hour.

Five additional test runs were conducted in Category II. ASTM E278 section 9.5.13 states:

If more than one test run is conducted at a specified burn rate, the results from at least two thirds

of the test runs in that burn rate category shall be used in calculating the weighted average

emission rate.

In accordance with this requirement, only four of the six (runs 3, 4, 5, and 6) Category II tests are

included in the weighted average. All measurement data and results from the other two runs

(runs 1 and 2) are included in this report.

The Viva L Series results are within the emission limit of 2.0 g/hr for affected facilities

manufactured on or after May 15, 2020.

The proportionality results for all eight test runs were acceptable. Quality check results for each

test run are presented in Section 4 of this report.




Denmark

TESTING NARRATIVE

Run 1 - To achieve a fuel loading density in accordance with the requirements of ASTM

E2780, using two different lengths of fuel piece was required. The fuel pieces in the

rear of the firebox were 10.5” in length and the front pieces were 12.5”. Targeted

category I burn rate at an air setting on 14mm open. Result of 1.04 kg/hr (category II).

Run 2 - Due to poor emissions performance in run 1, run 2 was performed with the same

settings and fuel sizes as a potential replacement run. Result of 0.86 kg/hr (category II).

Run 3 - During run 2 the size of the front fuel pieces, which spanned nearly 100% of the firebox

length, was observed impeding combustion airflow. It was then determined that if fuel

pieces very near to the 35 lb/ft3 density limit were used, loading density requirements

could be met with all five fuel pieces cut to the appropriate length of 10.5”. Run 3 and

all subsequent runs used this test fuel piece length.

Targeted category I at air setting of 15mm open. Result of 1.11 kg/hr (category II).

Run 4 - Targeted category I at an air setting of 13mm open. Result of 0.99 kg/hr (category II).

Run 5 - Repeat of run 4. Targeted category I at an air setting of 13mm open. Result of 0.93

kg/hr (category II).

Run 6 - Repeat of run 3. Targeted category II at an air setting of 15mm open. Result of 1.06

kg/hr (category II).

Run 7 - Targeted category III at an air setting of 22mm open. Result of 1.29 kg/hr (category

III).

Run 8 - Targeted category IV at primary air setting of fully open. Result of 1.73 kg/hr (category

III). Since no higher air adjustment is possible, this run is considered a category IV for

the purposes of reporting.

No sampling anomalies occurred during any run, and all proportionality results are acceptable, so

all test runs are valid for inclusion in the weighted average.

Since the lowest air setting used was 13mm open, a fixed stop at this setting will be included in

all production units. See drawing # 2728510USA for details.




Denmark

CATEGORY I BURN RATE RATIONALE

EPA Method 28 section 8.1.1.3.2 states the following:

Evidence that a wood heater cannot be operated at a burn rate less than 0.80

kg/hr shall include documentation of two or more attempts to operate the wood

heater in burn rate Category I and fuel combustion has stopped, or results of two

or more test runs demonstrating that the burn rates were greater than 0.80 kg/hr

when the air supply controls were adjusted to the lowest possible position or

settings… NOTE: After July 1, 1990, if a wood heater cannot be operated at a

burn rate less than 0.80 kg/hr, at least one test run with an average burn rate of

1.00 kg/hr or less shall be conducted.

The U.S. Environmental Protection Agency Applicability Determination Index, under Control

Number WDS-109, states the following regarding this requirement of Method 28:

The purpose of this requirement is to ensure that a good-faith effort has been

made to achieve a Category I burn rate. However, if the air supply control is

tamper-proof, EPA will accept one test as adequate documentation that the stove

cannot achieve a Category I burn rate. Note that this applies only to stoves which

do not reach the low burn rate because of limits on the air supply; manufacturers

of stoves which cannot sustain a burn rate at lower air settings will still be

required to submit documentation of two or more attempts. In all cases, a test

series consisting of at least four runs is required.

As the Run Notes in Section 3 and Table 10 in Section 1 of this report show, Runs 4 and 5 were

operated at a burn-rate of less than 1.0 kg/hr with the combustion air inlet open an area of 0.60

cm2. The primary air control was designed and manufactured with a stop that provides an area of

0.60 cm2 when the control is set to the minimum position. See attached drawings of the primary

air control system. The air controls for this heater are tamper-proof. When tested in accordance

with EPA Method 28 the heater cannot be induced to operate at a burn rate less than 0.80 kg/hr

therefore Runs 4 and 5 fulfill the requirements of the standard.




Denmark

Table 1 – Particulate Emissions

Run Burn Rate EPA 28R

Category

ASTM E2515 Emissions ASTM E2780

Weighting (kg/hr dry) (g/hr)

1 1.04 II 17.79 0.0%*

2 0.86 II 50.60 0.0%*

3 1.11 II 1.29 12.6%

4 0.99 II 0.79 5.9%

5 0.93 II 0.99 24.1%

6 1.06 II 0.90 5.9%

7 1.29 III 0.94 25.4%

8 1.73 IV 1.51 26.0%

Weighted Average of 6 test runs: 1.13 g/hr

*Runs 1 & 2 excluded from the weighted average per the requirements of EPA Method 28R/

ASTM E2780

Table 2 – Particulate Emissions (First Hour)

Run ASTM E2515

Emissions – First Hour

(g/hr)

1 46.19

2 60.91

3 3.12

4 1.08

5 1.58

6 0.70

7 0.59

8 1.02




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Table 3 – B415.1 Efficiency and CO Emissions

Run

Heat

Output

(BTU/hr)

HHV

Efficiency

(%)

LHV

Efficiency

(%)

CO Emissions

(g/MJ Output)

CO Emissions

(g/kg Dry Fuel)

CO Emissions

(g/hr)

1 12,285 63.0% 68.1% 21.16 264.21 274.00

2 9,150 57.2% 61.9% 31.59 358.23 304.74

3 14,587 70.8% 76.6% 9.97 139.86 153.27

4 13,175 72.2% 78.0% 8.54 122.08 118.59

5 12,490 72.6% 78.4% 8.68 124.84 114.32

6 13,820 71.9% 77.7% 8.14 115.93 118.61

7 17,028 73.0% 78.9% 4.99 72.19 89.63

8 22,857 71.7% 77.5% 4.51 64.12 108.79

Weighted average HHV efficiency of 6 test runs: 72.2%

Table 4 – Test Facility Conditions

Run

Room Temperature

(°F) Barometric Pressure

(in. Hg) Air Velocity

(ft/min)

Before After Before After Before After

1 70 71 29.72 29.79 <50 <50

2 71 71 29.89 29.89 <50 <50

3 69 67 29.83 29.77 <50 <50

4 70 70 29.51 29.50 <50 <50

5 72 71 29.53 29.61 <50 <50

6 69 72 29.96 29.99 <50 <50

7 71 71 30.02 30.09 <50 <50

8 72 71 30.29 30.24 <50 <50

Table 5 – Fuel Measurement and Crib Description Summary – PRETEST

Run Pretest Fuel Weight

(Starting weight in lbs) Pretest Moisture (Dry basis - %)

Coal Bed Weight (lbs)

1 9.2 22.91 2.1

2 9.3 20.89 2.1

3 8.8 19.72 2.1

4 8.3 20.81 2.0

5 8.3 21.45 2.1

6 8.3 20.92 1.7

7 8.7 20.75 2.1

8 9.5 21.11 1.7




Denmark

Table 6 – Fuel Measurement and Crib Description Summary – TEST

Run Test Fuel

Wet Basis

Test Fuel

Moisture

Test Fuel

Dry Basis

Fuel Loading

Density

Piece

Length 2x4s 4x4s

(lbs) (Dry basis %) (lbs) (Wet Basis lbs/ft3) (in) (count) (count)

1 8.4 22.50 6.88 6.51 10.5 & 12.5 5 0

2 8.4 22.19 6.95 6.51 10.5 & 12.5 5 0

3 8.2 19.83 6.92 6.36 10.5 5 0

4 8.2 20.95 6.92 6.36 10.5 5 0

5 8.2 21.89 6.84 6.36 10.5 5 0

6 8.3 22.69 7.01 6.43 10.5 5 0

7 8.4 22.79 7.10 6.51 10.5 5 0

8 8.3 21.07 7.00 6.43 10.5 5 0

Table 7 – Average Dilution Tunnel Gas Measurements

Run Static Pressure Flow Rate Temperature

(in. H2O) (dscf/min) (°F)

1 -0.28 196.14 85.6

2 -0.26 200.58 82.6

3 -0.26 196.16 87.1

4 -0.27 192.06 89.9

5 -0.27 194.13 89.4

6 -0.27 190.76 91.7

7 -0.27 192.84 96.4

8 -0.27 184.87 106.7

Table 8 - Average Temperature Data

Run Surface Delta T (F)*

1 8.2

2 64.6

3 44.0

4 56.2

5 64.6

6 56.6

7 80.2

8 42.0

*Represents the difference between

beginning and ending average surface

temperatures.




Denmark

Table 9 – Pretest Configuration

Run Combustion Air Fuel Added Fuel Removed Time (min)

1 14 mm Open None None 73







8 Fully Open None None 60

Table 10 – Test Configurations

Run Five-Minute Startup Procedures Combustion Air Setting

1

Fuel Loading: Completed by 0:40

Door: Closed at 0:50

Startup Air: Closed at 4:00

Primary Air: Closed from fully open to test setting from 4:30 – 5:00

14 mm Open

2





14 mm Open

3





15 mm Open

4





13 mm Open

5





13 mm Open

6





15 mm Open

7





22 mm Open

8




Primary Air: At test setting by 4:00

Fully Open




Denmark


Section 2

Photographs/Appliance Description/Drawings




Denmark


RAIS A/S

Viva L Series Test Dates: 2/6/2017 - 2/13/2017




Denmark


RAIS A/S

Viva L Series

Run 1 – Fuel Run 1 Newly Loaded Stove





Denmark


RAIS A/S

Viva L Series






Denmark


WOOD HEATER DESCRIPTION

Appliance Manufacturer: RAIS A/S

Wood Stove Model: Viva L Series

Type: Freestanding, radiant-type non-catalytic woodstove

WOOD HEATER INFORMATION

Materials of Construction: The unit is constructed primarily of mild steel. The firebox is lined

with formed vermiculite conforming to the unit’s cylindrical shape. The feed door has a 17”x16”

curved inner glass panel sealed with a ½” fiberglass rope gasket.

Air Introduction System: The wood heater has four air introduction systems: primary,

secondary, pilot, and auxiliary startup. The secondary and pilot systems are fixed and non-

adjustable, while the primary and auxiliary are user-adjustable via a single adjustment handle.

The primary air system draws air through the bottom of the unit and into the firebox via an

opening across the top of the loading door. The primary air control’s minimum setting

corresponds to an intake area of 0.06 cm2, and the area for the maximum setting is 7.84 cm2.

The secondary air system draws air through the bottom of the unit to intake holes in the back of

the firebox. Air is routed from these holes through the vermiculite firebox lining, with exit holes

into the firebox chamber in the rear of the firebox and in the front of the main baffle.

The pilot introduces air supplied by the secondary system to the firebox through a ¼” diameter

tube located in the lower rear of the firebox.

The auxiliary startup air draws air through the bottom of the firebox, and routes it into the

firebox through the ash grate. When the startup air system is open, the primary air intake area is

13.68 cm2.

Combustion Control Mechanisms: A single air slide handle controls both the auxiliary air and

primary air adjustment. Users are alerted to the point at which auxiliary air is fully closed and

primary air fully open by a positive-engagement point midway through the full range of

adjustment.

Internal Baffles: The unit features two vermiculite baffles to route flue gas. The main, lower

baffle contains secondary air holes, while the upper baffle is solid.

Other Features: The unit features an ash cleanout grate which empties into a removable

cleanout drawer located beneath the firebox. The grate includes a lower “shaker” grate which is

operated by a handle that can be accessed only while the loading door is open

Flue Outlet: The 6” diameter flue outlet is located at the top of the unit.





Model Variants: The Viva L series comes with several different options, for a total of 24

distinct variations. A full list of models can be found in the Engineering Drawings section. Each

option, and its effect on emissions performance, is summarized below:

Bi-metallic Air Control:

The Viva L models designated “CA” are specified with the “CleverAir” system, a thermostatic

control for the air damper that replaces the manual air control slide. A bi-metallic spring

mounted above the airbox, enclosed within the flue gas baffle, is permanently attached to the

linkage that actuates the air slide.

The fixed stops for minimum and maximum air settings remain in place, though the division

between primary and startup air is eliminated. However, the spring mimics the action of the

manual startup system by limiting air as the unit warms.

Models incorporating the CleverAir system have no user adjustment whatsoever. There is no air

slide, and owners are instructed to build and maintain the fire in accordance with flue draft and

coal bed conditions. The system is tamper-proof and located behind the firebox vermiculite,

preventing any unauthorized user interference with airflow.

Due to these design features of the system, no effect on emissions performance is anticipated.

Therefore Viva L “CA” models are included in this certification.

Side Glass Panels:

The Viva L models designated “G” can be specified with two fixed glass panels that flank the

feed door. In models without these panels, the firebox weldment and vermiculite extends all the

way to the feed door. Models with these panels feature an additional inner glass panel on the

loading door to compensate for the reduced heat capacity and increased radiant heat loss.

Viva L G Viva L Double Glass Door Single Glass Door

This option does not affect firebox volume or airflow, and the effects on emissions performance

by any variance in heat retention was carefully considered. The heat capacity and insulation

value of the additional steel and vermiculite are far greater than those of additional glass panel.

Therefore, the model with the side glass option was tested, and all variants are included in

certification.





Full Length Glass:

The loading door is available either with a front glass panel that extends the entire height of the

door, or a “Classic” version with a smaller glass panel enclosed in a steel door. This variation

does not affect the viewing (or volumetric) area of the firebox, nor does it impact heat capacity

or radiation. Therefore, both versions are included in certification as this option will not affect

emissions performance.

Viva L Classic Viva L

Taller Pedestal and Header:

The tested model, designated Viva “100” L, is 100cm tall. Two additional options, designated

“120” L and “160” L, are 120cm and 160 cm tall, respectively. These height increases are

achieved simply by extending the cylindrical body of the unit above and below the firebox. None

of the emissions control features of the design, such as air controls, baffles, or insulation, are

extended or raised. The dimensions of the firebox and airflow through the unit are not affected,

so these options have no impact on emissions performance. All variants are included in

certification.

Viva 100 L Viva 120 L Viva 160 L




Denmark


Section 3

Test Data by Run

OMNI-Test Laboratories, Inc. Page 1 of 1

EPA Weighted Average Emissions

EPA Method 28R

Client: RAIS Status: Final Stove Model: Viva L Stove Type: Non-Catalytic Stove

Test Dates: 2/6/2017 - 2/13/207

Project Number: 0138WS017E Emissions (g/hr): 1.1

Tracking Number: 2233 HHV Efficeincy (%): 72.2%

LHV Efficeincy (%): 78.0%

Run # 5 Run # 7Burn Rate (dry kg/hr) 0.93 Burn Rate (dry kg/hr) 1.29Category 2 Category 3LHV Efficiency (%) 0.784525057 LHV Efficiency (%) 0.774869834HHV Efficiency (%) 0.725861482 HHV Efficiency (%) 0.729867802Emissions (g/hr) 0.986120153 Emissions (g/hr) 0.943246237Weighting Factor 0.370 24.10% Weighting Factor 0.390 25.45%

Run # 4 Run # 8Burn Rate (dry kg/hr) 0.99 Burn Rate (dry kg/hr) 1.73Category 2 Category 3LHV Efficiency (%) 0.78007925 LHV Efficiency (%) 0.784525057HHV Efficiency (%) 0.721748114 HHV Efficiency (%) 0.716928238Emissions (g/hr) 0.793146295 Emissions (g/hr) 1.508187561Weighting Factor 0.090 5.88% Weighting Factor 0.399 26.03%

Run # 6

Burn Rate (dry kg/hr) 1.06Category 2LHV Efficiency (%) 0.765591654HHV Efficiency (%) 0.718823009Emissions (g/hr) 0.895296048Weighting Factor 0.090 5.90%

Run # 3Burn Rate (dry kg/hr) 1.11Category 2LHV Efficiency (%) 0.77691774HHV Efficiency (%) 0.708343841Emissions (g/hr) 1.290780152Weighting Factor 0.194 12.64%

Weighted Averages

0.00

0.20

0.40

0.60

0.80

1.00

1.20

1.40

1.60

0.00 0.50 1.00 1.50 2.00

Part

icula

te E

mis

sio

ns (

g/h

r)

Burn Rate (kg/hr dry)

Emission Rate Plot

Document Control No. P-SSF-0008 (EPA Method 28 Weighted Average Emissions).xls, Effective Date: 12/15/2010 Official Weighted Average.xlsm


Wood Heater Conditioning Data - ASTM E2780/ ASTM E2515

Manufacturer:

Model:

Tracking No.:

Project No.:

Test Date:

Technician:

Operation Category:

Elapsed Time

(hr)

Flue Gas

Temp

(° F)

Catalyst

Exit Temp

(° F)

Elapsed Time

(hr)

Flue Gas

Temp

(° F)

Catalyst

Exit Temp

(° F)

0 769.4 N/A 26 631.5 N/A

1 849.7 N/A 27 939.0 N/A

2 499.4 N/A 28 422.8 N/A

3 975.3 N/A 29 383.8 N/A

4 504.0 N/A 30 760.5 N/A

5 922.2 N/A 31 433.3 N/A

6 478.3 N/A 32 331.7 N/A

7 388.1 N/A 33 736.4 N/A

8 908.6 N/A 34 464.6 N/A

9 523.0 N/A 35 859.5 N/A

10 907.6 N/A 36 418.8 N/A

11 446.3 N/A 37 358.0 N/A

12 375.3 N/A 38 898.1 N/A

13 723.1 N/A 39 425.4 N/A

14 835.3 N/A 40 352.9 N/A

15 438.1 N/A 41 803.8 N/A

16 1040.0 N/A 42 482.4 N/A

17 480.9 N/A 43 960.2 N/A

18 424.6 N/A 44 499.3 N/A

19 750.7 N/A 45 836.5 N/A

20 480.8 N/A 46 477.3 N/A

21 384.1 N/A 47 915.5 N/A

22 780.5 N/A 48 493.3 N/A

23 913.9 N/A 49 767.3 N/A

24 416.5 N/A 50 436.2 N/A

25 364.0 N/A

Technician Signature:___________________________

II-III

RAIS

Viva L

2233

0138WS017E

12/21/16 - 1/6/17

Villy Jacobsen

Control No. P-SSAR-0002 Run 1 Emissions Sheet.xlsm

321

Small Sig




Denmark


Run 1


Wood Heater Preburn Data - ASTM E2780

Run: 1 Technician Signature:___________________________

Manufacturer:

Model:

Tracking No.: 9

Project No.: 9.2

Test Date:

Beginning Clock Time: 23.9 24.8 24.5

23.9 24.5 19.2

24.9 24.5 22.6

20.1 19.1

1.7 2.1 22.91

(min) (max)

Elapsed Time

(min)Scale (lb)

Stack Draft

(in H2O)FB Top FB Bottom FB Back FB Left FB Right

Avg.

Firebox

Surface

Stack Ambient

0 6.3 -0.038 491 285 281 266 306 325.7 306 68

10 5.6 -0.035 563 285 287 277 301 342.8 266 69

20 5.0 -0.036 596 277 291 288 308 351.8 280 69

30 4.1 -0.040 632 267 294 300 317 362.1 318 69

40 3.3 -0.041 669 257 303 310 327 373.3 344 69

50 2.6 -0.039 708 251 314 321 336 385.9 331 70

60 2.3 -0.030 681 249 326 332 347 387.1 256 70

70 2.2 -0.025 584 252 326 321 334 363.3 215 70

73 2.1 -0.023 556 253 323 312 327 354.0 207 70

Coal Bed

Range (lb):

Avg Preburn Moisture (% DB):

Fuel Moisture Readings (% DB):

Temperatures (°F)

2/6/2017

12:53

Fuel Piece Lengths (in.):

Total Preburn Weight (lb):

Preburn Fuel DataRAIS

Viva L

2233

0138WS017E


321

Small Sig


Manufacturer:

Model:

Tracking No.:

Project No.:

Test Date: 2/6/2017

Run No.: 1

1.29 6.9

11.7 29.40

8.4 6.51

0 N/A

1.68 - 2.1

Test Fuel

PieceWeight (lb) Size

Dry Weight

(lb)

1 1 2"x 4" 22.5 23.2 22.9 0.81

2 1.2 2"x 4" 23.1 22.5 22.9 0.98

3 1.2 2"x 4" 21.6 22.5 19.1 0.99

4 1.6 2"x 4" 24.2 22.1 19.9 1.31

5 1.4 2"x 4" 24.5 22.8 23.7 1.13

61.425

22.7 23.4 61.425

22.7 20.4 61.425

23.6 13.8 61.425

23.2 22.1 61.425

21.2 19.4 0

23.1 22.3 0

21.1 21.9 0

14.3 0

13.5 0

23.7 0

22.5 0

23.6

19.3


Spacer Readings (Dry Basis %)

Readings (Dry Basis %)

OK

OK

N/A

Coal Bed Range (20-25%):

Fuel Piece

Length (in):

Fuel Density

(lb/ft3, Dry Basis):

4x4 Crib

Weight (lb):

2x4 Crib

Weight (lb):

2x4 Percentage:

Loading Density

(lb/ft3, Wet Basis):

2233

Wood Heater Test Fuel Data - ASTM E2780

Viva L

0138WS017E

Firebox

Volume (ft3):

Total Fuel

Weight (Dry

Basis, lb):

RAIS


321

Small Sig


Wood Heater Test Data - ASTM E2780 / ASTM E2515

Run: 1

RAIS PM Control Modules: 335/336

Viva L Dilution Tunnel MW(dry): 29.00 lb/lb-mole Avg. Tunnel Velocity: 17.67 ft/sec.

2233 180 min Dilution Tunnel MW(wet): 28.78 lb/lb-mole Initial Tunnel Flow: 191.7 scfm Technician Signature:________________________________

0138WS017E Recording Interval: 10 min Dilution Tunnel H2O: 2.00 percent Average Tunnel Flow: 196.1 scfm

06-Feb-17 Dilution Tunnel Static: -0.280 "H2O Post-Test Leak Check (1): 0.000 cfm @ -5 in. Hg

Beginning Clock Time: 14:07 Background Sample Volume: 0 cubic feet Tunnel Area: 0.19635 ft2 Post-Test Leak Check (2): 0.000 cfm @ -5 in. Hg

Pitot Tube Cp: 0.99 Average Test Piece Fuel Moisture: 22.50 Dry Basis %

Meter Box Y Factor: 0.984 (1) 0.99 (2) 1 (Amb)

Barometric Pressure: Begin Middle End Average Pt.1 Pt.2 Pt.3 Pt.4 Pt.5 Pt.6 Pt.7 Pt.8 Center

29.72 29.75 29.79 29.75 "Hg Initial dP 0.052 0.070 0.080 0.060 0.052 0.076 0.080 0.062 0.088 "H2O

OMNI Equipment Numbers: 296-T55, 185, 340, 431, 335, 336, 594, 410, 559, 209, 132, 23, 592, 283A Temp: 92 92 92 92 92 92 92 92 92 °F

Vstrav 17.78 ft/sec Vscent 20.18 ft/sec Fp 0.881

Particulate Sampling Data

Elapsed

Time

(min)

Gas

Meter 1

(ft3)

Gas

Meter 2

(ft3)

Sample

Rate 1 (cfm)

Sample

Rate 2

(cfm)

Orifice

dH 1

("H2O)

Meter 1

Temp

(°F)

Meter 1

Vacuum

("Hg)

Orifice

dH 2

("H2O)

Meter 2

Temp

(°F)

Meter 2

Vacuum

("Hg)

Dilution

Tunnel

(°F)

Dilution

Tunnel

Center

dP

Pro.

Rate 1

Pro.

Rate 2

Scale

Reading

Weight

Change

Firebox

Top

Firebox

Bottom

Firebox

Back

Firebox

Left

Firebox

Right

Avg.

Stove

Surface

Temp

Catalyst

Exit TempStack Filter 1 Dryer Exit 1 Filter 2 Dryer Exit 2 Ambient

Draft

("H2O)

CO2

(%)

CO

(%)

0 0.000 0.000 0.85 73 1.84 0.68 74 1.2 97 0.088 8.4 545 253 322 310 329 352 N/A 266 68 68 68 68 70 -0.032 1.72 0.54

10 1.666 1.688 0.17 0.17 1.35 74 2.14 1.21 74 1.3 85 0.088 102 101 7.7 -0.7 484 275 300 271 282 322 N/A 225 70 70 70 70 69 -0.027 2.47 1.45

20 3.312 3.389 0.16 0.17 1.35 75 2.15 1.20 76 1.3 82 0.088 100 101 7.3 -0.4 418 296 293 244 256 301 N/A 189 70 70 70 70 69 -0.022 2.88 1.78

30 4.959 5.089 0.16 0.17 1.33 77 2.15 1.19 77 1.3 80 0.088 100 100 6.8 -0.5 374 298 285 232 246 287 N/A 183 70 70 70 70 69 -0.021 4.18 1.86

40 6.605 6.788 0.16 0.17 1.34 78 2.17 1.19 78 1.4 80 0.088 99 100 6.3 -0.5 359 293 282 230 246 282 N/A 187 70 70 70 70 69 -0.021 3.79 2.53

50 8.249 8.483 0.16 0.17 1.33 79 2.2 1.18 79 1.4 83 0.088 99 100 5.3 -1 401 286 283 239 255 293 N/A 260 71 71 71 71 69 -0.034 8.53 2.73

60 9.891 10.175 0.16 0.17 1.32 80 2.22 1.18 80 1.4 86 0.088 99 100 4.3 -1 506 278 292 265 279 324 N/A 287 71 71 71 71 70 -0.035 10.33 2.83

70 11.546 11.865 0.17 0.17 1.33 81 2.17 1.17 81 1.4 89 0.088 100 100 3.3 -1 585 270 302 286 305 350 N/A 309 72 72 72 72 70 -0.038 11.64 1.74

80 13.200 13.557 0.17 0.17 1.33 81 2.18 1.17 81 1.4 91 0.088 100 100 2.5 -0.8 638 262 314 304 322 368 N/A 304 73 73 73 73 70 -0.036 10.25 2.25

90 14.854 15.248 0.17 0.17 1.33 82 2.18 1.18 82 1.4 90 0.088 100 100 1.9 -0.6 677 255 323 318 335 382 N/A 284 73 73 73 73 71 -0.033 9.12 0.81

100 16.508 16.941 0.17 0.17 1.34 83 2.19 1.18 83 1.4 89 0.088 100 100 1.5 -0.4 616 251 328 321 340 371 N/A 242 73 73 73 73 71 -0.028 5.93 3.25

110 18.165 18.635 0.17 0.17 1.34 83 2.19 1.18 83 1.4 87 0.088 100 100 1.3 -0.2 578 250 334 323 338 365 N/A 242 73 73 73 73 72 -0.026 7.57 0.82

120 19.824 20.332 0.17 0.17 1.35 83 2.19 1.18 84 1.4 86 0.088 100 100 1.1 -0.2 553 253 346 328 351 366 N/A 228 73 73 73 73 71 -0.024 7.41 0.76

130 21.484 22.029 0.17 0.17 1.34 84 2.2 1.19 84 1.4 85 0.088 100 99 0.9 -0.2 527 260 352 334 350 365 N/A 218 73 73 73 73 72 -0.022 7.11 0.95

140 23.145 23.728 0.17 0.17 1.34 84 2.19 1.19 84 1.4 84 0.088 100 99 0.8 -0.1 507 268 354 333 349 362 N/A 215 73 73 73 73 71 -0.022 7 1.08

150 24.806 25.427 0.17 0.17 1.34 84 2.19 1.18 84 1.4 84 0.088 100 99 0.6 -0.2 493 275 358 333 348 361 N/A 212 72 72 72 72 71 -0.021 6.72 1.31

160 26.468 27.126 0.17 0.17 1.35 84 2.19 1.18 84 1.4 83 0.088 100 99 0.5 -0.1 481 282 361 335 346 361 N/A 210 72 72 72 72 71 -0.021 6.71 1.45

170 28.130 28.825 0.17 0.17 1.35 84 2.2 1.19 84 1.4 83 0.088 100 99 0.3 -0.2 472 288 363 335 346 361 N/A 205 72 72 72 72 71 -0.020 6.52 1.27

180 29.793 30.524 0.17 0.17 1.35 84 2.19 1.19 84 1.4 83 0.088 100 99 0.0 -0.3 466 293 363 331 347 360 N/A 204 72 72 72 72 71 -0.020 7.39 0.91

Avg/Tot 29.793 30.524 0.17 0.17 1.31 81 1.16 81 86 0.088 100 100 8.2 72 72 72 70 -0.026

Test Date:

Stack Gas DataFuel Weight (lb) Temperature Data (°F)

Velocity Traverse Data

Manufacturer:

Model:

Tracking No.: Total Sampling Time:

Project No.:

Export to


321

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Wood Heater Test Results - ASTM E2780 / ASTM E2515

Manufacturer: RAIS

Model: Viva L

Project No.: 0138WS017E

Tracking No.: 2233

Run: 1

Test Date:

Burn Rate 1.04 kg/hr dry

Average Tunnel Temperature 86 degrees Fahrenheit

Average Gas Velocity in Dilution Tunnel - vs 17.67 feet/second

Average Gas Flow Rate in Dilution Tunnel - Qsd 11768.2 dscf/hour

Average Delta p 0.088 inches H20

Total Time of Test 180 minutes

Total Sample Volume - Vm 0.000 cubic feet 29.793 cubic feet 30.524 cubic feet 9.891 cubic feet

Average Gas Meter Temperature 70 degrees Fahrenheit 81 degrees Fahrenheit 81 degrees Fahrenheit 81 degrees Fahrenheit

Total Sample Volume (Standard Conditions) - Vmstd 0.000 dscf 28.550 dscf 29.409 dscf 9.478 dscf

Total Particulates - mn 0 mg 43.5 mg 44.1 mg 37.2 mg

Particulate Concentration (dry-standard) - Cr/Cs 0.000000 grams/dscf 0.00152 grams/dscf 0.00150 grams/dscf 0.00392 grams/dscf

Total Particulate Emissions - ET 0.00 grams 53.79 grams 52.94 grams 46.19 grams

Particulate Emission Rate 0.00 grams/hour 17.93 grams/hour 17.65 grams/hour 46.19 grams/hour

Emissions Factor 17.24 g/kg 16.97 g/kg 30.42 g/kg

Difference from Average Total Particulate Emissions 0.43 grams 0.43 grams

Complete Test Run

Total Particulate Emissions - ET 53.37 grams

Particulate Emission Rate 17.79 grams/hour

Emissions Factor 17.10 grams/kg

First Hour Emissions




Technician Signature:_____________________________________________________

Stove Surface ∆T OK

OK

Filter Face Velocity (47 mm)

Dryer Exit Temp < 80F

Leakage Rate

Ambient Temp (55-90°F)

Negative Probe Weight Eval.

OKPro-Rate Variation

OK

Filter Temps < 90 °F OK

OK

OK

OK

02/06/17

SAMPLE TRAIN 1 SAMPLE TRAIN 2AMBIENT

QUALITY CHECKSFINAL AVERAGE RESULTS

FIRST HOUR FILTER (TRAIN 1)

Dual Train Comparison Results Are Acceptable

321

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Manufacturer: RAIS Technicians:

Model: Viva L

Date: 02/06/17

Run: 1

Control #: 0138WS017E

Test Duration: 180

Output Category: II

HHV Basis LHV Basis

Overall Efficiency 63.0% 68.1%

Combustion Efficiency 80.8% 80.8%

Heat Transfer Efficiency 78% 84.3%

Output Rate (kJ/h) 12,950 12,285 (Btu/h)

Burn Rate (kg/h) 1.04 2.29 (lb/h)

Input (kJ/h) 20,544 19,489 (Btu/h)

Test Load Weight (dry kg) 3.11 6.86 dry lb

MC wet (%) 18.37

MC dry (%) 22.50

Particulate (g ) N/A

CO (g) 822

Test Duration (h) 3.00

Emissions Particulate CO

g/MJ Output N/A 21.16

g/kg Dry Fuel N/A 264.21

g/h N/A 274.00

lb/MM Btu Output N/A 49.17

Air/Fuel Ratio (A/F) 14.65

VERSION: 2.2 12/14/2009

OMNI-Test Laboratories

Test Results in Accordance with CSA B415.1-09

321

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Denmark


Run 2




Manufacturer:

Model:

Tracking No.: 8

Project No.: 9.3

Test Date:


18.9 20.6 19.1

22.2 24.3 19.2

22.9 22.8

1.7 2.1 20.89

(min) (max)

Elapsed Time

(min)Scale (lb)

Stack Draft


Avg.

Firebox

Surface

Stack Ambient

0 7.2 -0.052 609 359 333 343 318 392.5 454 70

10 5.8 -0.047 664 371 353 344 333 413 399 72

20 4.9 -0.040 680 361 367 345 346 419.6 329 71

30 3.9 -0.046 708 342 372 348 352 424.4 396 72

40 3.1 -0.044 743 323 369 346 351 426.5 387 71

50 2.6 -0.039 725 308 371 358 355 423.3 319 71

60 2.2 -0.033 675 300 374 362 366 415.3 275 72

67 2.1 -0.030 637 300 374 360 368 408.1 257 72

Coal Bed

Range (lb):



Temperatures (°F)

2/7/2017

11:19




Viva L

2233

0138WS017E


321

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Manufacturer:

Model:

Tracking No.:

Project No.:

Test Date: 2/7/2017

Run No.: 2

1.29 7.0

11.7 28.98

8.4 6.51

0 N/A

1.68 - 2.1

Test Fuel


Dry Weight

(lb)

1 0.9 2"x 4" 20.1 20.2 19.7 0.75

2 1.2 2"x 4" 23.2 22.6 22.6 0.98

3 1.3 2"x 4" 23.8 23.4 23.2 1.05

4 1.4 2"x 4" 23.9 22.1 22.7 1.14

5 1.5 2"x 4" 22.3 22.8 20.2 1.23

61.425

20.2 12.6 61.425

19.7 19.2 61.425

15.1 17.0 61.425

16.7 18.9 61.425

19.9 19.8 0

13.9 13.0 0

18.5 15.0 0

17.0 0

12.2 0

17.3 0

16.8 0

16.7

12.6




OK

OK

N/A


Fuel Piece

Length (in):

Fuel Density


4x4 Crib

Weight (lb):

2x4 Crib

Weight (lb):

2x4 Percentage:

Loading Density


2233


Viva L

0138WS017E

Firebox

Volume (ft3):

Total Fuel

Weight (Dry

Basis, lb):

RAIS


321

Small Sig



Run: 2





07-Feb-17 Dilution Tunnel Static: -0.260 "H2O Post-Test Leak Check (1): 0.000 cfm @ 12 in. Hg

Beginning Clock Time: 12:33 Background Sample Volume: 0 cubic feet Tunnel Area: 0.19635 ft2 Post-Test Leak Check (2): 0.000 cfm @ 11 in. Hg




29.89 29.89 29.89 29.89 "Hg Initial dP 0.048 0.080 0.082 0.068 0.044 0.070 0.080 0.060 0.095 "H2O




Elapsed

Time

(min)

Gas

Meter 1

(ft3)

Gas

Meter 2

(ft3)

Sample

Rate 1 (cfm)

Sample

Rate 2

(cfm)

Orifice

dH 1

("H2O)

Meter 1

Temp

(°F)

Meter 1

Vacuum

("Hg)

Orifice

dH 2

("H2O)

Meter 2

Temp

(°F)

Meter 2

Vacuum

("Hg)

Dilution

Tunnel

(°F)

Dilution

Tunnel

Center

dP

Pro.

Rate 1

Pro.

Rate 2

Scale

Reading

Weight

Change

Firebox

Top

Firebox

Bottom

Firebox

Back

Firebox

Left

Firebox

Right

Avg.

Stove

Surface

Temp

Catalyst


Draft

("H2O)

CO2

(%)

CO

(%)

0 0.000 0.000 0.03 75 1.85 0.67 76 1.3 105 0.090 8.4 631 299 375 359 370 407 N/A 327 71 71 70 70 71 -0.038 2.81 0.23

10 1.699 1.698 0.17 0.17 1.44 76 2.29 1.22 77 1.3 90 0.090 106 107 7.6 -0.8 590 331 358 318 326 385 N/A 270 73 73 73 73 71 -0.034 3.17 0.91

20 3.399 3.403 0.17 0.17 1.43 77 2.29 1.20 78 1.3 86 0.090 106 107 7.1 -0.5 502 349 337 287 295 354 N/A 215 73 73 73 73 71 -0.027 3.41 1.41

30 5.097 5.108 0.17 0.17 1.42 79 2.29 1.20 79 1.3 84 0.100 100 101 6.7 -0.4 438 344 318 268 276 329 N/A 198 72 72 73 73 71 -0.024 4.28 1.85

40 6.796 6.810 0.17 0.17 1.41 80 2.31 1.19 80 1.4 82 0.100 99 101 6.2 -0.5 402 336 307 257 264 313 N/A 191 72 72 72 72 70 -0.022 4.78 2.26

50 8.492 8.508 0.17 0.17 1.41 81 2.33 1.18 81 1.4 82 0.100 99 100 5.7 -0.5 390 329 305 255 264 309 N/A 195 72 72 72 72 70 -0.022 5.99 1.73

60 10.186 10.195 0.17 0.17 1.43 81 2.28 1.15 81 1.5 82 0.100 99 100 5.0 -0.7 388 324 307 258 264 308 N/A 196 72 72 72 72 70 -0.021 5.04 3.23

70 11.894 11.861 0.17 0.17 1.42 82 2.31 1.13 82 1.6 81 0.100 99 98 4.3 -0.7 377 319 312 261 266 307 N/A 197 72 72 72 72 70 -0.021 5.50 3.78

80 13.596 13.512 0.17 0.17 1.41 82 2.34 1.17 82 1.7 82 0.100 99 97 3.5 -0.8 378 315 320 270 273 311 N/A 201 72 72 72 72 70 -0.021 5.80 4.23

90 15.291 15.193 0.17 0.17 1.40 82 2.37 1.15 82 1.8 82 0.100 99 99 2.8 -0.7 387 311 333 286 292 322 N/A 198 72 72 72 72 70 -0.021 5.78 4.34

100 16.979 16.860 0.17 0.17 1.39 82 2.4 1.13 82 1.9 81 0.100 98 98 2.2 -0.6 396 309 344 299 306 331 N/A 193 72 72 72 72 71 -0.020 5.59 4.22

110 18.664 18.518 0.17 0.17 1.39 82 2.41 1.13 82 1.9 81 0.100 98 98 1.8 -0.4 403 308 348 304 314 335 N/A 185 72 72 72 72 70 -0.019 4.95 3.95

120 20.350 20.178 0.17 0.17 1.39 82 2.4 1.13 82 1.9 80 0.100 98 98 1.7 -0.1 404 307 347 308 314 336 N/A 174 71 71 71 71 70 -0.018 4.52 3.69

130 22.037 21.840 0.17 0.17 1.40 82 2.4 1.14 82 1.9 80 0.100 98 98 1.5 -0.2 400 306 346 307 312 334 N/A 170 70 70 71 71 69 -0.017 4.65 3.71

140 23.726 23.505 0.17 0.17 1.40 82 2.4 1.14 82 1.9 80 0.100 98 98 1.4 -0.1 398 305 344 305 311 333 N/A 170 70 70 71 71 70 -0.016 4.78 3.84

150 25.413 25.169 0.17 0.17 1.40 82 2.4 1.14 82 1.9 80 0.090 103 103 1.2 -0.2 398 303 342 302 308 331 N/A 173 71 71 71 71 70 -0.017 4.65 3.98

160 27.101 26.833 0.17 0.17 1.40 82 2.4 1.14 82 1.8 80 0.100 98 98 1.0 -0.2 408 302 332 297 303 328 N/A 177 71 71 71 71 69 -0.017 6.83 1.17

170 28.789 28.500 0.17 0.17 1.39 82 2.4 1.14 82 1.9 80 0.100 98 98 0.9 -0.1 421 300 328 294 304 329 N/A 179 70 70 71 71 70 -0.017 6.82 1.15

180 30.477 30.163 0.17 0.17 1.39 82 2.4 1.14 82 1.8 80 0.090 104 103 0.7 -0.2 427 300 327 296 306 331 N/A 178 71 71 71 71 70 -0.016 7.00 1.08

190 32.164 31.828 0.17 0.17 1.40 82 2.4 1.14 82 1.8 81 0.100 98 98 0.6 -0.1 435 301 329 299 311 335 N/A 182 71 71 71 71 70 -0.017 7.30 1.03

200 33.851 33.493 0.17 0.17 1.39 82 2.41 1.14 82 1.8 81 0.100 98 98 0.4 -0.2 439 303 334 304 315 339 N/A 183 71 71 71 71 70 -0.017 7.13 1.23

210 35.538 35.159 0.17 0.17 1.38 83 2.41 1.14 82 1.9 80 0.100 98 98 0.2 -0.2 440 305 338 307 318 342 N/A 182 71 71 71 71 71 -0.017 6.98 1.25

220 37.226 36.825 0.17 0.17 1.40 83 2.41 1.14 83 1.8 80 0.100 98 98 0.0 -0.2 439 308 338 307 319 342 N/A 182 71 71 71 71 71 -0.018 6.99 1.38

Avg/Tot 37.226 36.825 0.17 0.17 1.34 81 1.13 81 83 0.098 100 100 64.6 71 72 72 70 -0.021

Test Date:



Manufacturer:

Model:


Project No.:

Export to


321

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Manufacturer: RAIS

Model: Viva L


Tracking No.: 2233

Run: 2

Test Date:










Total Particulates - mn 0 mg 150 mg 150.4 mg 49.6 mg






Complete Test Run










OK



Leakage Rate




OK


OK

OK

OK

02/07/17





321

Small Sig


Model: Viva L

Date: 02/07/17

Run: 2


Test Duration: 220

Output Category: II

HHV Basis LHV Basis






Input (kJ/h) 16,852 15,986 (Btu/h)


MC wet (%) 18.16

MC dry (%) 22.19

Particulate (g ) n/a

CO (g) 1,117





g/h N/A 304.74



VERSION: 2.2 12/14/2009



321

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Denmark


Run 3




Manufacturer:

Model:

Tracking No.: 8

Project No.: 8.8

Test Date:


18.6 19.5 20.1

19.6 18.9 19.3

19.7 19.1

1.6 2.1 19.72

(min) (max)

Elapsed Time

(min)

Scale

(lb)

Stack Draft


Avg.

Firebox

Surface

Stack Ambient

0 8.4 -0.062 573 325 331 341 332 325.7 479 69

10 7.4 -0.05 581 355 329 313 311 342.8 322 69

20 6.4 -0.05 617 341 329 310 305 351.8 346 68

30 5.5 -0.05 660 317 333 320 311 362.1 353 69

40 4.6 -0.048 681 294 338 331 320 373.3 340 69

50 3.7 -0.047 685 277 340 342 327 385.9 332 68

60 3 -0.047 692 270 345 350 334 387.1 331 69

70 2.5 -0.043 687 269 348 355 337 363.3 306 68

80 2.2 -0.037 639 272 354 350 345 392 265 69

83 2.1 -0.034 625 274 357 351 347 390.8 259 68

Coal Bed

Range (lb):



Temperatures (°F)

2/8/2017

12:57




Viva L

2233

0138WS017E


321

Small Sig


Manufacturer:

Model:

Tracking No.:

Project No.:

Test Date: 2/8/2017

Run No.: 3

1.29 6.9

10.5 29.82

8.2 6.36

0 N/A

1.64 - 2.05

Test Fuel


Dry Weight

(lb)

1 1.1 2"x 4" 19.4 19.1 19.5 0.92

2 1.1 2"x 4" 19.4 19.0 19.1 0.92

3 1.2 2"x 4" 20.3 19.4 19.1 1.00

4 1.2 2"x 4" 20.5 19.7 20.2 1.00

5 1.1 2"x 4" 19.8 21.6 21.3 0.91

55.125

17.8 55.125

12.2 55.125

14.6 55.125

8.8 55.125

19.1 0

17.6 0

17.7 0

19.9 0

14.3 0

16.1 0

0




OK

OK

N/A


Fuel Piece

Length (in):

Fuel Density


4x4 Crib

Weight (lb):

2x4 Crib

Weight (lb):

2x4 Percentage:

Loading Density


2233


Viva L

0138WS017E

Firebox

Volume (ft3):

Total Fuel

Weight (Dry

Basis, lb):

RAIS


321

Small Sig



Run: 3










29.83 29.8 29.77 29.80 "Hg Initial dP 0.052 0.074 0.078 0.052 0.044 0.070 0.074 0.062 0.097 "H2O




Elapsed

Time

(min)

Gas

Meter 1

(ft3)

Gas

Meter 2

(ft3)

Sample

Rate 1 (cfm)

Sample

Rate 2

(cfm)

Orifice

dH 1

("H2O)

Meter 1

Temp

(°F)

Meter 1

Vacuum

("Hg)

Orifice

dH 2

("H2O)

Meter 2

Temp

(°F)

Meter 2

Vacuum

("Hg)

Dilution

Tunnel

(°F)

Dilution

Tunnel

Center

dP

Pro.

Rate 1

Pro.

Rate 2

Scale

Reading

Weight

Change

Firebox

Top

Firebox

Bottom

Firebox

Back

Firebox

Left

Firebox

Right

Avg.

Stove

Surface

Temp

Catalyst


Draft

("H2O)

CO2

(%)

CO

(%)

0 0.000 0.000 0.41 73 0.61 0.11 74 -0.4 100 0.095 8.2 619 274 358 351 350 390 N/A 313 67 68 67 68 69 -0.045 4.02 0.37

10 1.697 1.670 0.17 0.17 1.44 73 2.29 1.18 74 1.3 92 0.102 100 100 7.0 -1.2 620 313 342 320 316 382 N/A 343 70 70 71 70 68 -0.049 9.82 1.15

20 3.393 3.341 0.17 0.17 1.44 75 2.28 1.16 76 1.3 92 0.102 100 100 6.0 -1 648 336 333 305 301 385 N/A 348 71 70 72 70 68 -0.050 10.03 1.74

30 5.091 5.011 0.17 0.17 1.43 76 2.28 1.16 77 1.3 92 0.100 101 101 4.9 -1.1 672 334 326 312 305 390 N/A 344 71 70 73 70 68 -0.050 11.11 1.99

40 6.789 6.682 0.17 0.17 1.43 78 2.29 1.16 78 1.3 94 0.101 100 100 3.8 -1.1 707 323 326 324 312 398 N/A 389 71 70 73 70 69 -0.054 12.37 2.39

50 8.490 8.355 0.17 0.17 1.43 79 2.29 1.16 79 1.3 97 0.101 100 100 2.7 -1.1 752 310 331 338 323 411 N/A 416 72 71 74 71 69 -0.055 12.86 0.42

60 10.194 10.029 0.17 0.17 1.43 80 2.27 1.16 80 1.3 95 0.100 100 101 2.0 -0.7 768 300 341 352 335 419 N/A 364 72 71 74 71 69 -0.049 9.79 0.45

70 11.901 11.706 0.17 0.17 1.43 80 2.27 1.16 81 1.3 91 0.099 101 101 1.7 -0.3 714 293 354 365 343 414 N/A 290 72 72 73 72 68 -0.040 8.54 0.42

80 13.611 13.385 0.17 0.17 1.43 81 2.27 1.17 81 1.3 87 0.099 100 100 1.4 -0.3 645 292 359 365 347 402 N/A 261 71 73 73 73 68 -0.035 7.51 0.88

90 15.323 15.065 0.17 0.17 1.44 81 2.26 1.16 82 1.3 85 0.103 98 98 1.3 -0.1 585 300 357 360 343 389 N/A 240 71 73 72 73 69 -0.032 7.18 1.18

100 17.037 16.747 0.17 0.17 1.44 81 2.27 1.16 81 1.3 83 0.102 99 99 1.1 -0.2 540 310 354 354 336 379 N/A 225 70 73 71 73 69 -0.030 6.93 1.44

110 18.750 18.428 0.17 0.17 1.44 81 2.26 1.17 81 1.3 82 0.099 100 100 1.0 -0.1 510 320 349 348 329 371 N/A 216 70 73 71 73 69 -0.027 6.65 1.47

120 20.465 20.111 0.17 0.17 1.45 81 2.27 1.17 81 1.3 81 0.102 99 99 0.8 -0.2 486 329 346 338 322 364 N/A 211 69 73 71 73 68 -0.027 6.4 1.58

130 22.181 21.795 0.17 0.17 1.44 81 2.27 1.17 81 1.3 80 0.099 100 100 0.7 -0.1 467 336 343 329 316 358 N/A 207 69 73 70 73 68 -0.026 6.23 1.3

140 23.897 23.479 0.17 0.17 1.44 81 2.27 1.17 81 1.3 80 0.099 100 100 0.5 -0.2 454 339 340 325 313 354 N/A 204 69 73 70 73 67 -0.025 6.43 1.26

150 25.611 25.163 0.17 0.17 1.44 80 2.26 1.17 81 1.3 79 0.101 99 99 0.4 -0.1 447 339 337 324 310 351 N/A 202 69 72 70 72 67 -0.025 6.24 1.45

160 27.327 26.845 0.17 0.17 1.44 80 2.26 1.17 81 1.3 79 0.101 99 99 0.2 -0.2 441 338 336 319 309 349 N/A 201 69 72 70 72 68 -0.025 6.17 1.49

170 29.043 28.528 0.17 0.17 1.44 80 2.26 1.17 80 1.3 79 0.102 99 99 0.0 -0.2 439 335 334 317 307 346 N/A 201 69 72 69 72 67 -0.025 6.38 1.4

Avg/Tot 29.043 28.528 0.17 0.17 1.38 79 1.11 79 87 0.100 100 100 44.0 72 71 72 68 -0.037

Test Date:



Manufacturer:

Model:


Project No.:

Export to

Control No. P-SSAR-0002 Page 3 of 6 Run 3 Emissions Sheet.xlsm

321

Small Sig

321

Rectangle


Manufacturer: RAIS

Model: Viva L


Tracking No.: 2233

Run: 3

Test Date:
















Complete Test Run








7.5% of Average Total Particulate Emissions 0.27 grams



OK



Leakage Rate




OK


OK

OK

OK

02/08/17





321

Small Sig


Model: Viva L

Date: 02/08/17

Run: 3


Test Duration: 170

Output Category: II

HHV Basis LHV Basis






Input (kJ/h) 21,709 20,593 (Btu/h)


MC wet (%) 16.55

MC dry (%) 19.83


CO (g) 434





g/h N/A 153.27



VERSION: 2.2 12/14/2009



321

Small Sig




Denmark


Run 4




Manufacturer:

Model:

Tracking No.: 8.0

Project No.: 8.3

Test Date:


22.4 19.4 19.6

21.9 22.6 21.7

19.9 20.4

1.6 2.1 20.81

(min) (max)

Elapsed Time

(min)Scale (lb)

Stack Draft


Avg.

Firebox

Surface

Stack Ambient

0 8.8 -0.041 440 155 232 268 251 269.2 315 68

0 7.6 -0.052 462 258 271 259 251 300.3 381 68

10 6.6 -0.048 530 304 297 270 258 331.9 325 68

20 5.6 -0.05 598 306 299 293 281 355.3 349 69

30 4.7 -0.045 653 297 306 316 300 374.4 322 69

40 4.0 -0.045 676 289 313 327 314 383.7 313 68

50 3.1 -0.047 695 283 324 337 322 392.1 340 69

60 2.5 -0.041 707 280 339 350 333 401.6 306 70

70 2.0 -0.036 687 278 345 361 341 402.5 271 70

72 2.0 -0.035 678 277 345 358 341 399.9 263 70

Coal Bed

Range (lb):



Temperatures (°F)

2/9/2017

9:15




Viva L

2233

0138WS017E


321

Small Sig


Manufacturer:

Model:

Tracking No.:

Project No.:

Test Date: 2/9/2017

Run No.: 4

1.29 6.922

10.5 29.56

8.2 6.36

0 N/A

1.64 - 2.05

Test Fuel


Dry Weight

(lb)

1 1.1 2"x 4" 23.6 23.0 21.5 0.90

2 1.1 2"x 4" 19.9 22.7 24.5 0.90

3 1.2 2"x 4" 19.2 19.0 19.1 1.01

4 1.2 2"x 4" 19.9 22.4 21.0 0.99

5 1.1 2"x 4" 19.7 19.6 19.1 0.92

55.125

8.1 13.4 55.125

8.7 8.9 55.125

9.3 14.1 55.125

8.8 8.8 55.125

16.7 12.8 0

17.9 12.9 0

17.0 17.1 0

12.2 17.0 0

17.0 14.4 0

12.8 17.6 0

0




OK

OK

N/A


Fuel Piece

Length (in):

Fuel Density


4x4 Crib

Weight (lb):

2x4 Crib

Weight (lb):

2x4 Percentage:

Loading Density


2233


Viva L

0138WS017E

Firebox

Volume (ft3):

Total Fuel

Weight (Dry

Basis, lb):

RAIS


321

Small Sig



Run: 4










29.51 29.51 29.50 29.51 "Hg Initial dP 0.048 0.070 0.076 0.058 0.044 0.076 0.076 0.056 0.098 "H2O




Elapsed

Time

(min)

Gas

Meter 1

(ft3)

Gas

Meter 2

(ft3)

Sample

Rate 1 (cfm)

Sample

Rate 2

(cfm)

Orifice

dH 1

("H2O)

Meter 1

Temp

(°F)

Meter 1

Vacuum

("Hg)

Orifice

dH 2

("H2O)

Meter 2

Temp

(°F)

Meter 2

Vacuum

("Hg)

Dilution

Tunnel

(°F)

Dilution

Tunnel

Center

dP

Pro.

Rate 1

Pro.

Rate 2

Scale

Reading

Weight

Change

Firebox

Top

Firebox

Bottom

Firebox

Back

Firebox

Left

Firebox

Right

Avg.

Stove

Surface

Temp

Catalyst


Draft

("H2O)

CO2

(%)

CO

(%)

0 0.000 0.000 0.03 73 0.04 0.27 73 0.0 106 0.098 8.2 669 277 345 356 343 398.0 N/A 341 68 68 68 68 70 -0.048 4.05 0.24

10 1.673 1.661 0.17 0.17 1.40 74 2.23 1.15 74 1.3 94 0.102 99 99 7.2 -1.0 638 311 338 319 308 382.8 N/A 328 71 71 72 72 70 -0.047 8.55 0.46

20 3.356 3.327 0.17 0.17 1.39 76 2.21 1.14 76 1.3 93 0.098 101 101 6.4 -0.8 647 331 333 304 293 381.6 N/A 311 72 72 73 73 71 -0.045 8.98 0.36

30 5.039 4.994 0.17 0.17 1.39 77 2.20 1.14 78 1.3 93 0.098 101 101 5.7 -0.7 665 327 318 297 291 379.6 N/A 309 72 72 73 73 70 -0.044 9.85 0.69

40 6.725 6.663 0.17 0.17 1.39 79 2.21 1.14 79 1.3 96 0.098 101 101 4.7 -1.0 680 317 318 303 298 383.2 N/A 375 73 73 74 74 70 -0.051 12.74 0.88

50 8.413 8.335 0.17 0.17 1.38 80 2.21 1.14 81 1.3 98 0.098 101 101 3.6 -1.1 715 307 330 320 312 396.8 N/A 382 73 73 74 74 70 -0.052 11.52 3.9

60 10.103 10.006 0.17 0.17 1.38 81 2.21 1.14 82 1.3 99 0.100 100 100 2.6 -1.0 741 297 345 336 328 409.4 N/A 386 73 73 75 75 70 -0.053 11.86 2.4

70 11.794 11.680 0.17 0.17 1.38 82 2.21 1.14 82 1.3 96 0.096 102 102 1.9 -0.7 754 289 357 357 344 420.2 N/A 329 74 74 75 75 71 -0.044 9.09 0.44

80 13.489 13.357 0.17 0.17 1.39 82 2.22 1.14 83 1.3 92 0.098 101 100 1.6 -0.3 692 284 364 368 352 412.0 N/A 269 74 74 75 75 71 -0.036 7.79 0.49

90 15.185 15.036 0.17 0.17 1.39 83 2.22 1.15 83 1.3 90 0.098 100 100 1.4 -0.2 630 284 364 366 350 398.8 N/A 245 73 73 74 74 71 -0.033 7.32 0.6

100 16.883 16.716 0.17 0.17 1.39 83 2.22 1.15 84 1.3 87 0.097 101 100 1.2 -0.2 575 290 361 359 346 386.2 N/A 227 73 73 74 74 71 -0.029 6.7 1.02

110 18.581 18.398 0.17 0.17 1.39 83 2.21 1.15 84 1.3 85 0.100 99 99 1.1 -0.1 532 299 353 350 338 374.4 N/A 215 73 73 73 73 70 -0.027 6.54 0.95

120 20.282 20.081 0.17 0.17 1.40 83 2.21 1.14 83 1.3 85 0.099 100 100 1.0 -0.1 500 309 346 339 328 364.4 N/A 210 72 72 73 73 70 -0.025 6.82 0.91

130 21.982 21.763 0.17 0.17 1.39 83 2.22 1.14 83 1.3 84 0.100 99 99 0.8 -0.2 480 316 341 332 321 358.0 N/A 203 72 72 72 72 70 -0.024 6.44 1.05

140 23.681 23.446 0.17 0.17 1.40 83 2.21 1.15 83 1.3 84 0.102 98 98 0.7 -0.1 466 321 337 327 318 353.8 N/A 201 72 72 72 72 70 -0.024 6.69 1.08

150 25.382 25.128 0.17 0.17 1.40 83 2.21 1.15 83 1.3 84 0.096 101 101 0.6 -0.1 457 323 335 325 315 351.0 N/A 196 72 72 72 72 70 -0.023 6.38 1.22

160 27.081 26.810 0.17 0.17 1.39 83 2.21 1.14 83 1.3 83 0.098 100 100 0.4 -0.2 448 324 332 320 312 347.2 N/A 195 72 72 72 72 70 -0.023 6.37 1.3

170 28.782 28.494 0.17 0.17 1.39 83 2.22 1.15 83 1.3 83 0.100 99 99 0.3 -0.1 442 324 330 319 310 345.0 N/A 195 72 72 72 72 70 -0.023 6.24 1.34

180 30.484 30.178 0.17 0.17 1.40 83 2.22 1.14 83 1.3 83 0.100 99 99 0.1 -0.2 439 324 329 315 309 343.2 N/A 194 72 72 72 72 70 -0.023 6.06 1.46

190 32.183 31.861 0.17 0.17 1.39 83 2.22 1.15 83 1.3 83 0.105 96 97 0.0 -0.1 437 324 329 312 307 341.8 N/A 195 72 72 72 72 70 -0.023 5.94 1.33

Avg/Tot 32.183 31.861 0.17 0.17 1.32 81 1.10 81 90 0.099 100 100 56.2 72 73 73 70 -0.035

Test Date:



Manufacturer:

Model:


Project No.:

Export to


321

Small Sig

321

Rectangle


Manufacturer: RAIS

Model: Viva L


Tracking No.: 2233

Run: 4

Test Date:
















Complete Test Run










OK



Leakage Rate




OK


OK

OK

OK

02/09/17





321

Small Sig


Model: Viva L

Date: 02/09/17

Run: 4


Test Duration: 190

Output Category: II

HHV Basis LHV Basis






Input (kJ/h) 19,244 18,255 (Btu/h)


MC wet (%) 17.32

MC dry (%) 20.95


CO (g) 376





g/h N/A 118.59



VERSION: 2.2 12/14/2009



321

Small Sig




Denmark


Run 5




Manufacturer:

Model:

Tracking No.: 8.0

Project No.: 8.3

Test Date:


19.7 22.2 23.8

24.3 18.6 20.1

22.1 19.9

1.6 2.1 21.45

(min) (max)

Elapsed Time

(min)Scale (lb)

Stack Draft


Avg.

Firebox

Surface

Stack Ambient

0 7.9 -0.057 579 387 328 319 321 386.9 440 71

10 7.1 -0.042 568 403 331 314 311 385.4 278 72

20 6.2 -0.046 576 381 320 310 306 378.6 307 71

30 5.2 -0.043 613 354 325 325 322 387.7 298 71

40 4.5 -0.042 651 333 327 331 330 394.5 293 71

50 3.7 -0.044 674 317 329 335 334 397.7 316 72

60 3.0 -0.043 692 303 337 344 337 402.8 303 71

70 2.5 -0.04 692 292 346 354 344 405.7 289 72

80 2.2 -0.035 666 286 347 358 343 400.0 259 72

83 2.1 -0.034 651 285 347 357 340 396.0 252 72




Viva L

2233

0138WS017E

Coal Bed

Range (lb):



Temperatures (°F)

2/9/2017

14:18


321

Small Sig


Manufacturer:

Model:

Tracking No.:

Project No.:

Test Date: 2/9/2017

Run No.: 5

1.29 6.843

10.5 29.32

8.2 6.36

0 N/A

1.64 - 2.05

Test Fuel


Dry Weight

(lb)

1 1.1 2"x 4" 20.9 22.5 22.8 0.90

2 1.1 2"x 4" 23.3 21.2 21.3 0.90

3 1.2 2"x 4" 22.4 23.9 21.1 0.98

4 1.2 2"x 4" 22.1 21.7 21.1 0.99

5 1.1 2"x 4" 21.4 22.5 20.1 0.91

55.125

19.3 14.6 55.125

14.8 12.8 55.125

19.1 19.5 55.125

18.3 9.9 55.125

11.7 16.0 0

8.9 13.3 0

20.1 15.0 0

14.1 18.8 0

13.6 12.7 0

20.4 14.9 0

0


2233


Viva L

0138WS017E

Firebox

Volume (ft3):

Total Fuel

Weight (Dry

Basis, lb):

RAIS



OK

OK

N/A


Fuel Piece

Length (in):

Fuel Density


4x4 Crib

Weight (lb):

2x4 Crib

Weight (lb):

2x4 Percentage:

Loading Density



321

Small Sig



Run: 5










29.53 29.56 29.61 29.57 "Hg Initial dP 0.048 0.070 0.076 0.058 0.044 0.076 0.076 0.056 0.098 "H2O




Elapsed

Time

(min)

Gas

Meter 1

(ft3)

Gas

Meter 2

(ft3)

Sample

Rate 1 (cfm)

Sample

Rate 2

(cfm)

Orifice

dH 1

("H2O)

Meter 1

Temp

(°F)

Meter 1

Vacuum

("Hg)

Orifice

dH 2

("H2O)

Meter 2

Temp

(°F)

Meter 2

Vacuum

("Hg)

Dilution

Tunnel

(°F)

Dilution

Tunnel

Center

dP

Pro.

Rate 1

Pro.

Rate 2

Scale

Reading

Weight

Change

Firebox

Top

Firebox

Bottom

Firebox

Back

Firebox

Left

Firebox

Right

Avg.

Stove

Surface

Temp

Catalyst


Draft

("H2O)

CO2

(%)

CO

(%)

0 0.000 0.000 0.03 77 1.88 0.17 0.18 77.0 108 0.097 8.2 645 285 347 356 341 394.8 N/A 313 70 70 70 70 72 -0.045 3.89 0.29

10 1.685 1.673 0.17 0.17 1.40 77 2.26 0.17 1.16 78.0 96 0.099 102 101 7.2 -1.0 613 316 340 319 307 379.0 N/A 315 73 73 74 74 72 -0.046 9.35 1.09

20 3.370 3.345 0.17 0.17 1.39 79 2.25 0.17 1.14 79.0 93 0.100 101 100 6.4 -0.8 608 336 343 302 296 377.0 N/A 293 74 74 74 74 71 -0.044 9.62 0.92

30 5.055 5.017 0.17 0.17 1.38 80 2.24 0.17 1.14 80.0 93 0.098 102 101 5.5 -0.9 631 333 340 300 297 380.2 N/A 320 74 74 75 75 71 -0.047 11.45 2.13

40 6.741 6.691 0.17 0.17 1.38 81 2.25 0.17 1.15 81.0 95 0.101 100 100 4.6 -0.9 661 323 333 308 304 385.8 N/A 354 74 74 75 75 71 -0.051 13.13 0.63

50 8.430 8.367 0.17 0.17 1.38 82 2.24 0.17 1.15 82.0 98 0.103 99 99 3.6 -1.0 702 312 332 321 311 395.6 N/A 408 74 74 75 75 70 -0.056 14.11 1.61

60 10.120 10.045 0.17 0.17 1.39 82 2.25 0.17 1.15 83.0 99 0.099 102 102 2.7 -0.9 744 302 335 333 322 407.2 N/A 403 74 74 75 75 71 -0.055 13.91 0.95

70 11.812 11.723 0.17 0.17 1.39 83 2.25 0.17 1.15 84.0 95 0.103 99 99 2.0 -0.7 760 293 340 349 332 414.8 N/A 343 74 74 75 75 71 -0.049 10.34 0.16

80 13.507 13.404 0.17 0.17 1.39 83 2.25 0.17 1.15 84.0 92 0.102 100 100 1.7 -0.3 714 287 347 358 343 409.8 N/A 272 74 74 74 74 72 -0.039 8.77 0.31

90 15.202 15.087 0.17 0.17 1.39 83 2.24 0.17 1.16 84.0 87 0.106 97 97 1.5 -0.2 646 286 353 361 344 398.0 N/A 239 73 73 73 73 70 -0.034 7.13 1.15

100 16.900 16.772 0.17 0.17 1.39 83 2.24 0.17 1.15 84.0 85 0.103 99 99 1.4 -0.1 585 292 350 352 335 382.8 N/A 220 72 72 73 73 70 -0.031 7.15 1.17

110 18.596 18.457 0.17 0.17 1.40 83 2.24 0.17 1.15 83.0 84 0.100 100 100 1.2 -0.2 540 298 347 341 329 371.0 N/A 207 72 72 72 72 70 -0.027 6.64 1.51

120 20.295 20.141 0.17 0.17 1.39 83 2.25 0.17 1.15 83.0 84 0.102 99 99 1.1 -0.1 503 303 343 334 320 360.6 N/A 200 72 72 72 72 70 -0.025 6.72 1.38

130 21.991 21.826 0.17 0.17 1.40 83 2.24 0.17 1.16 83.0 84 0.101 99 100 0.9 -0.2 478 309 339 327 317 354.0 N/A 192 72 72 72 72 70 -0.024 6.77 1.35

140 23.689 23.512 0.17 0.17 1.40 83 2.25 0.17 1.15 83.0 84 0.098 101 101 0.8 -0.1 464 314 335 321 315 349.8 N/A 190 72 72 73 73 71 -0.023 6.34 1.48

150 25.386 25.197 0.17 0.17 1.40 83 2.25 0.17 1.15 83.0 84 0.105 98 98 0.7 -0.1 450 316 332 315 311 344.8 N/A 188 72 72 73 73 71 -0.022 6.18 1.62

160 27.085 26.881 0.17 0.17 1.40 83 2.25 0.17 1.16 83.0 83 0.101 99 100 0.6 -0.1 441 316 330 311 308 341.2 N/A 183 72 72 73 73 71 -0.021 6.25 1.72

170 28.782 28.565 0.17 0.17 1.39 83 2.24 0.17 1.15 84.0 83 0.099 100 101 0.4 -0.2 431 316 328 308 306 337.8 N/A 183 72 72 73 73 71 -0.021 5.99 1.93

180 30.480 30.250 0.17 0.17 1.40 84 2.24 0.17 1.15 84.0 84 0.100 100 100 0.3 -0.1 423 316 325 305 303 334.4 N/A 180 72 72 73 73 71 -0.021 6.16 1.86

190 32.178 31.935 0.17 0.17 1.40 84 2.25 0.17 1.15 84.0 83 0.102 99 99 0.2 -0.1 419 316 323 304 301 332.6 N/A 180 72 72 73 73 72 -0.020 6.39 1.68

200 33.877 33.619 0.17 0.17 1.40 84 2.24 0.17 1.15 84 83 0.100 100 100 0.0 -0.2 415 315 321 300 300 330 N/A 179 72 72 73 73 71 -0.021 4.86 3.22

Avg/Tot 33.877 33.619 0.17 0.17 1.33 82 0.17 1 89 0.101 100 100 64.6 73 73 73 71 -0.034

Manufacturer:

Model:


Project No.:

Test Date:


Velocity Traverse DataExport to


321

Small Sig

321

Rectangle


Manufacturer: RAIS

Model: Viva L


Tracking No.: 2233

Run: 5

Test Date:
















Complete Test Run









02/09/17






OK

OK

OK


OK



Leakage Rate




OK

321

Small Sig


Model: Viva L

Date: 02/09/17

Run: 5


Test Duration: 200

Output Category: II

HHV Basis LHV Basis






Input (kJ/h) 18,141 17,208 (Btu/h)


MC wet (%) 17.96

MC dry (%) 21.89


CO (g) 381





g/h N/A 114.32



VERSION: 2.2 12/14/2009



321

Small Sig




Denmark


Run 6




Manufacturer:

Model:

Tracking No.: 8.0

Project No.: 8.3

Test Date:

Beginning Clock Time: 18.7 22.8

20.3 19.6

19.3 19.3

25.4 19.5

24.9 19.4

1.7 2.1 20.92

(min) (max)

Elapsed Time

(min)Scale (lb)

Stack Draft


Avg.

Firebox

Surface

Stack Ambient

0 8.6 -0.044 454 130 225 261 255 265.0 309 68

10 7.2 -0.064 452 234 259 255 247 289.4 480 68

20 5.8 -0.054 575 297 293 286 273 344.6 369 68

30 4.6 -0.051 636 301 309 313 310 373.8 348 68

40 3.7 -0.049 681 293 326 332 329 392.2 337 68

50 3.0 -0.046 700 285 339 346 342 402.4 319 68

60 2.3 -0.044 694 280 348 358 348 405.7 309 68

70 1.9 -0.041 667 280 350 359 361 403.4 292 68

74 1.7 -0.041 658 280 352 358 359 401.5 281 68

Coal Bed

Range (lb):



Temperatures (°F)

2/10/2017

8:54




Viva L

2233

0138WS017E


321

Small Sig


Manufacturer:

Model:

Tracking No.:

Project No.:

Test Date: 2/10/2017

Run No.: 6

1.29 7.008

10.5 29.12

8.3 6.43

0 N/A

1.66 - 2.075

Test Fuel


Dry Weight

(lb)

1 1.2 2"x 4" 23.7 23.1 22.9 0.97

2 1.1 2"x 4" 19.8 22.4 22.6 0.90

3 1.1 2"x 4" 22.5 22.5 22.5 0.90

4 1.1 2"x 4" 23.1 23.3 23.3 0.89

5 1.2 2"x 4" 23.7 22.5 22.5 0.98

55.125

7.6 9.4 55.125

18.3 10.2 55.125

6.8 7.6 55.125

8.0 11.3 55.125

6.9 8.8 0

8.8 9.6 0

11.2 7.9 0

14.3 0

8.2 0

12.1 0

11.3 0

9.7

13.1




OK

OK

N/A


Fuel Piece

Length (in):

Fuel Density


4x4 Crib

Weight (lb):

2x4 Crib

Weight (lb):

2x4 Percentage:

Loading Density


2233


Viva L

0138WS017E

Firebox

Volume (ft3):

Total Fuel

Weight (Dry

Basis, lb):

RAIS


321

Small Sig



Run: 6










29.96 29.98 29.99 29.98 "Hg Initial dP 0.056 0.076 0.074 0.056 0.044 0.072 0.072 0.056 0.103 "H2O




Elapsed

Time

(min)

Gas

Meter 1

(ft3)

Gas

Meter 2

(ft3)

Sample

Rate 1 (cfm)

Sample

Rate 2

(cfm)

Orifice

dH 1

("H2O)

Meter 1

Temp

(°F)

Meter 1

Vacuum

("Hg)

Orifice

dH 2

("H2O)

Meter 2

Temp

(°F)

Meter 2

Vacuum

("Hg)

Dilution

Tunnel

(°F)

Dilution

Tunnel

Center

dP

Pro.

Rate 1

Pro.

Rate 2

Scale

Reading

Weight

Change

Firebox

Top

Firebox

Bottom

Firebox

Back

Firebox

Left

Firebox

Right

Avg.

Stove

Surface

Temp

Catalyst


Draft

("H2O)

CO2

(%)

CO

(%)

0 0.000 0.000 0.52 72 1.14 0.78 73 1.3 105 0.102 8.3 654 280 353 362 363 402.4 N/A 327 68 68 68 68 69 -0.050 4.07 0.29

10 1.672 1.661 0.17 0.17 1.43 72 2.29 1.17 73 1.3 95 0.100 101 101 7.1 -1.2 645 316 346 322 323 390.4 N/A 353 70 70 72 72 68 -0.051 9.84 1.26

20 3.354 3.328 0.17 0.17 1.41 74 2.27 1.16 75 1.3 95 0.101 100 100 6.1 -1.0 664 338 341 305 307 391.0 N/A 336 71 71 73 73 69 -0.050 10.26 1

30 5.036 4.995 0.17 0.17 1.41 76 2.28 1.16 77 1.3 97 0.099 101 101 5.0 -1.1 689 335 332 307 308 394.2 N/A 370 72 72 73 73 70 -0.053 11.86 0.96

40 6.720 6.665 0.17 0.17 1.41 78 2.28 1.16 78 1.3 100 0.101 100 100 4.0 -1.0 718 326 331 320 317 402.4 N/A 411 73 73 74 74 70 -0.056 13.29 0.65

50 8.406 8.334 0.17 0.17 1.41 79 2.27 1.17 80 1.3 104 0.100 101 101 2.9 -1.1 760 314 335 337 328 414.8 N/A 435 74 74 75 75 70 -0.058 13.36 1.01

60 10.095 10.007 0.17 0.17 1.41 80 2.27 1.17 81 1.3 101 0.103 99 99 2.1 -0.8 783 303 341 352 338 423.4 N/A 378 74 74 76 76 71 -0.053 11.42 0.17

70 11.797 11.684 0.17 0.17 1.42 81 2.26 1.16 82 1.3 95 0.100 101 100 1.7 -0.4 725 296 350 367 350 417.6 N/A 284 74 74 75 75 71 -0.040 3.49 3.3

80 13.495 13.362 0.17 0.17 1.42 82 2.26 1.17 83 1.3 91 0.101 99 99 1.5 -0.2 614 294 352 355 347 392.4 N/A 254 74 74 75 75 71 -0.036 7.61 0.62

90 15.196 15.043 0.17 0.17 1.42 82 2.26 1.17 83 1.3 89 0.096 102 102 1.3 -0.2 565 300 350 352 351 383.6 N/A 234 74 74 74 74 71 -0.032 6.75 0.93

100 16.897 16.725 0.17 0.17 1.43 83 2.26 1.17 83 1.3 87 0.101 99 99 1.1 -0.2 528 311 350 349 348 377.2 N/A 221 73 73 74 74 71 -0.029 7.28 0.83

110 18.598 18.407 0.17 0.17 1.42 83 2.26 1.17 84 1.3 87 0.102 98 98 1.0 -0.1 509 320 348 341 339 371.4 N/A 219 73 73 74 74 71 -0.028 7.06 0.86

120 20.303 20.090 0.17 0.17 1.43 83 2.26 1.17 84 1.3 86 0.099 100 100 0.8 -0.2 497 326 346 338 336 368.6 N/A 216 73 73 73 73 71 -0.027 6.79 1.06

130 22.007 21.775 0.17 0.17 1.43 83 2.27 1.17 84 1.3 85 0.100 99 99 0.7 -0.1 484 331 345 335 330 365.0 N/A 212 72 72 73 73 71 -0.027 6.4 1.22

140 23.710 23.458 0.17 0.17 1.42 83 2.26 1.17 84 1.3 85 0.099 100 100 0.5 -0.2 472 334 342 330 326 360.8 N/A 210 72 72 73 73 72 -0.026 6.29 1.3

150 25.413 25.141 0.17 0.17 1.43 83 2.27 1.17 84 1.3 86 0.100 100 99 0.4 -0.1 462 335 339 326 321 356.6 N/A 206 72 72 73 73 72 -0.025 6.31 1.15

160 27.117 26.825 0.17 0.17 1.43 83 2.27 1.17 84 1.3 85 0.101 99 99 0.2 -0.2 453 337 337 326 317 354.0 N/A 203 72 72 73 73 71 -0.025 5.07 1.26

170 28.821 28.509 0.17 0.17 1.42 84 2.27 1.17 84 1.3 85 0.100 99 99 0.1 -0.1 439 339 334 317 314 348.6 N/A 198 73 73 73 73 72 -0.025 5.79 1.11

180 30.524 30.192 0.17 0.17 1.42 84 2.26 1.17 84 1.3 85 0.099 100 100 0.0 -0.1 428 342 331 314 314 345.8 N/A 194 73 73 73 73 72 -0.023 5.92 1.08

Avg/Tot 30.524 30.192 0.17 0.17 1.37 80 1.15 81 92 0.100 100 100 56.6 72 73 73 71 -0.038

Test Date:



Manufacturer:

Model:


Project No.:

Export to


321

Small Sig

321

Rectangle


Manufacturer: RAIS

Model: Viva L


Tracking No.: 2233

Run: 6

Test Date:
















Complete Test Run










OK



Leakage Rate




OK


OK

OK

OK

02/10/17





321

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Model: Viva L

Date: 02/10/17

Run: 6


Test Duration: 180

Output Category: II

HHV Basis LHV Basis






Input (kJ/h) 20,268 19,226 (Btu/h)


MC wet (%) 18.50

MC dry (%) 22.69


CO (g) 356





g/h N/A 118.61



VERSION: 2.2 12/14/2009



321

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Denmark


Run 7




Manufacturer:

Model:

Tracking No.: 8.0

Project No.: 8.7

Test Date:


20.0 22.0 21.6

19.8 22.0 21.3

20.8 18.6

1.7 2.1 20.75

(min) (max)

Elapsed Time

(min)Scale (lb)

Stack Draft


Avg.

Firebox

Surface

Stack Ambient

0 8.9 -0.052 597 320 336 364 357 394.7 356 72

10 7.7 -0.057 607 373 336 332 323 394.2 396 70

20 6.3 -0.059 656 370 331 333 329 403.7 403 70

30 5.1 -0.058 702 346 339 350 351 417.5 407 71

40 4.0 -0.062 756 325 350 366 359 431.3 451 71

50 3.1 -0.056 762 309 361 381 370 436.6 393 71

60 2.4 -0.054 735 301 376 397 404 442.6 387 71

68 2.1 -0.047 697 303 394 407 397 439.7 335 71

Coal Bed

Range (lb):



Temperatures (°F)

2/10/2017

14:44




Viva L

2233

0138WS017E


321

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Manufacturer:

Model:

Tracking No.:

Project No.:


Run No.: 7

1.29 7.097

10.5 30.13

8.4 6.51

0 N/A

1.68 - 2.1

Test Fuel


Dry Weight

(lb)

1 1.2 2"x 4" 22.8 23.0 22.5 0.98

2 1.2 2"x 4" 22.7 22.5 22.7 0.98

3 1.2 2"x 4" 23.0 23.1 23.5 0.97

4 1.1 2"x 4" 23.1 23.2 23.9 0.89

5 1.2 2"x 4" 22.6 21.2 22.1 0.98

55.125

8.0 8.9 55.125

8.4 9.8 55.125

7.0 11.2 55.125

7.4 8.0 55.125

13.2 8.8 0

8.2 7.7 0

9.9 8.0 0

8.0 11.5 0

11.5 7.8 0

7.8 10.3 0

0




OK

OK

N/A


Fuel Piece

Length (in):

Fuel Density


4x4 Crib

Weight (lb):

2x4 Crib

Weight (lb):

2x4 Percentage:

Loading Density


2233


Viva L

0138WS017E

Firebox

Volume (ft3):

Total Fuel

Weight (Dry

Basis, lb):

RAIS


321

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Run: 7










30.02 30.07 30.09 30.06 "Hg Initial dP 0.056 0.076 0.074 0.056 0.044 0.072 0.072 0.056 0.103 "H2O




Elapsed

Time

(min)

Gas

Meter 1

(ft3)

Gas

Meter 2

(ft3)

Sample

Rate 1 (cfm)

Sample

Rate 2

(cfm)

Orifice

dH 1

("H2O)

Meter 1

Temp

(°F)

Meter 1

Vacuum

("Hg)

Orifice

dH 2

("H2O)

Meter 2

Temp

(°F)

Meter 2

Vacuum

("Hg)

Dilution

Tunnel

(°F)

Dilution

Tunnel

Center

dP

Pro.

Rate 1

Pro.

Rate 2

Scale

Reading

Weight

Change

Firebox

Top

Firebox

Bottom

Firebox

Back

Firebox

Left

Firebox

Right

Avg.

Stove

Surface

Temp

Catalyst


Draft

("H2O)

CO2

(%)

CO

(%)

0 0.000 0.000 0.03 76 1.68 0.40 78 1.0 112 0.104 8.4 688 302 396 408 397 438.2 N/A 365 69 69 70 70 71 -0.053 3.35 0.2

10 1.686 1.668 0.17 0.17 1.43 77 2.31 1.18 78 1.4 102 0.104 100 100 7.1 -1.3 680 342 380 359 351 422.4 N/A 411 73 73 74 74 71 -0.060 10.94 0.67

20 3.374 3.337 0.17 0.17 1.42 78 2.30 1.17 79 1.3 104 0.100 102 102 5.7 -1.4 719 358 366 338 332 422.6 N/A 452 74 74 75 75 70 -0.064 12.34 0.99

30 5.061 5.005 0.17 0.17 1.41 79 2.29 1.17 80 1.4 106 0.104 100 100 4.4 -1.3 764 348 354 345 338 429.8 N/A 473 74 74 75 75 70 -0.065 13.63 1.07

40 6.749 6.676 0.17 0.17 1.42 80 2.30 1.17 81 1.3 108 0.110 97 98 3.1 -1.3 802 332 350 356 347 437.4 N/A 499 75 75 76 76 70 -0.066 14.16 0.31

50 8.439 8.347 0.17 0.17 1.41 80 2.29 1.16 82 1.4 103 0.104 100 100 2.2 -0.9 806 316 353 375 357 441.4 N/A 426 75 75 75 75 71 -0.059 11.33 0.14

60 10.133 10.020 0.17 0.17 1.43 81 2.26 1.17 83 1.4 99 0.100 101 101 1.7 -0.5 755 307 363 393 375 438.6 N/A 349 74 74 75 75 70 -0.049 8.57 0.06

70 11.834 11.694 0.17 0.17 1.43 82 2.25 1.17 83 1.4 95 0.103 100 100 1.4 -0.3 675 303 380 403 388 429.8 N/A 304 75 75 75 75 71 -0.044 7.47 0.4

80 13.538 13.370 0.17 0.17 1.44 83 2.25 1.17 84 1.4 92 0.101 101 100 1.2 -0.2 613 307 389 397 394 420.0 N/A 283 74 74 74 74 72 -0.039 7.3 0.59

90 15.243 15.048 0.17 0.17 1.43 83 2.25 1.17 84 1.4 91 0.103 100 99 1.0 -0.2 571 314 388 387 396 411.2 N/A 270 74 74 74 74 71 -0.037 7.19 0.81

100 16.948 16.727 0.17 0.17 1.43 83 2.26 1.17 84 1.4 90 0.104 99 99 0.8 -0.2 541 322 384 377 390 402.8 N/A 260 74 74 74 74 71 -0.035 6.83 0.98

110 18.655 18.407 0.17 0.17 1.43 84 2.26 1.17 85 1.4 89 0.102 100 100 0.6 -0.2 522 327 381 373 371 394.8 N/A 251 73 73 74 74 71 -0.035 6.64 0.98

120 20.362 20.088 0.17 0.17 1.44 84 2.26 1.17 85 1.4 88 0.101 100 100 0.5 -0.1 505 330 371 361 353 384.0 N/A 245 73 73 74 74 72 -0.034 6.13 1

130 22.071 21.769 0.17 0.17 1.44 84 2.26 1.17 85 1.4 88 0.100 101 101 0.3 -0.2 487 332 356 349 340 372.8 N/A 244 73 73 74 74 71 -0.033 5.79 1.27

140 23.779 23.450 0.17 0.17 1.44 84 2.26 1.17 85 1.4 88 0.103 99 99 0.1 -0.2 473 333 348 337 331 364.4 N/A 240 73 73 73 73 72 -0.033 5.85 1.2

150 25.488 25.131 0.17 0.17 1.44 84 2.26 1.17 84 1.4 88 0.105 98 98 0.0 -0.1 461 337 340 328 324 358.0 N/A 237 73 73 74 74 71 -0.032 5.76 1.11

Avg/Tot 25.488 25.131 0.17 0.17 1.34 81 1.12 83 96 0.103 100 100 80.2 74 74 74 71 -0.046

Test Date:



Manufacturer:

Model:


Project No.:

Export to


321

Small Sig

321

Rectangle


Manufacturer: RAIS

Model: Viva L


Tracking No.: 2233

Run: 7

Test Date:
















Complete Test Run










OK



Leakage Rate




OK


OK

OK

OK

02/10/17





321

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Model: Viva L

Date: 02/10/17

Run: 7


Test Duration: 150

Output Category: II

HHV Basis LHV Basis






Input (kJ/h) 24,594 23,331 (Btu/h)


MC wet (%) 18.56

MC dry (%) 22.79


CO (g) 224





g/h N/A 89.63



VERSION: 2.2 12/14/2009



321

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Denmark


Run 8




Manufacturer:

Model:

Tracking No.: 8.0

Project No.: 9.5

Test Date:


19.4 18.6

23.6 24.2

22.1 22.1

18.4 21

1.7 2.1 21.11

(min) (max)

Elapsed Time

(min)Scale (lb)

Stack Draft


Avg.

Firebox

Surface

Stack Ambient

0 8.9 -0.062 457 211 257 272 264 292.5 424 70

10 7.4 -0.067 582 277 280 277 287 340.7 476 69

20 5.8 -0.069 678 297 301 312 327 382.9 497 70

30 4.1 -0.071 761 300 330 349 364 420.7 547 71

40 2.8 -0.066 782 304 360 387 398 446.2 511 70

50 2.0 -0.059 754 317 390 430 420 462.1 433 71

60 1.7 -0.051 673 348 413 434 413 456.0 364 71




Viva L

2233

0138WS017E

Coal Bed

Range (lb):



Temperatures (°F)

2/13/2017

10:37


321

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Manufacturer:

Model:

Tracking No.:

Project No.:


Run No.: 8

1.29 6.995

10.5 29.00

8.3 6.43

0 N/A

1.66 - 2.075

Test Fuel


Dry Weight

(lb)

1 1.2 2"x 4" 19.8 21.1 21.2 0.99

2 1.1 2"x 4" 22.6 22.4 21.8 0.90

3 1.1 2"x 4" 21.5 20.3 21.9 0.91

4 1.1 2"x 4" 21.0 21.3 19.7 0.91

5 1.1 2"x 4" 20.1 22.1 19.3 0.91

55.125

11.4 14.4 55.125

14.8 13.6 55.125

12.7 12.4 55.125

11.2 13.6 55.125

14.0 12.3 0

15.8 12.7 0

14.3 13.7 0

15.5 12.1 0

16.4 0

14.5 0

16.4 0

17.0


2233


Viva L

0138WS017E

Firebox

Volume (ft3):

Total Fuel

Weight (Dry

Basis, lb):

RAIS



OK

OK

N/A


Fuel Piece

Length (in):

Fuel Density


4x4 Crib

Weight (lb):

2x4 Crib

Weight (lb):

2x4 Percentage:

Loading Density



321

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Run: 8










30.29 30.27 30.24 30.27 "Hg Initial dP 0.048 0.080 0.074 0.060 0.048 0.074 0.076 0.058 0.062 "H2O




Elapsed

Time

(min)

Gas

Meter 1

(ft3)

Gas

Meter 2

(ft3)

Sample

Rate 1 (cfm)

Sample

Rate 2

(cfm)

Orifice

dH 1

("H2O)

Meter 1

Temp

(°F)

Meter 1

Vacuum

("Hg)

Orifice

dH 2

("H2O)

Meter 2

Temp

(°F)

Meter 2

Vacuum

("Hg)

Dilution

Tunnel

(°F)

Dilution

Tunnel

Center

dP

Pro.

Rate 1

Pro.

Rate 2

Scale

Reading

Weight

Change

Firebox

Top

Firebox

Bottom

Firebox

Back

Firebox

Left

Firebox

Right

Avg.

Stove

Surface

Temp

Catalyst


Draft

("H2O)

CO2

(%)

CO

(%)

0 0.000 0.000 0.46 75 0.93 0.03 77 1.3 115 0.066 8.3 666 350 414 430 414 454.8 N/A 375 70 70 71 71 72 -0.054 2.85 0.25

10 1.677 1.667 0.17 0.17 1.44 76 2.32 1.20 77 1.4 110 0.057 103 104 6.8 -1.5 673 398 389 367 365 438.4 N/A 456 74 74 75 75 71 -0.065 11.45 0.76

20 3.359 3.340 0.17 0.17 1.42 77 2.32 1.18 79 1.4 117 0.061 100 101 5.2 -1.6 731 412 379 353 352 445.4 N/A 505 75 75 77 77 72 -0.069 12.96 0.97

30 5.039 5.011 0.17 0.17 1.41 79 2.33 1.17 81 1.4 126 0.058 103 104 3.6 -1.6 797 399 385 371 371 464.6 N/A 570 77 77 80 80 73 -0.074 14.82 0.63

40 6.715 6.678 0.17 0.17 1.40 81 2.35 1.17 83 1.4 125 0.060 101 102 2.2 -1.4 825 383 398 408 394 481.6 N/A 526 79 79 80 80 73 -0.069 12.7 0.34

50 8.392 8.341 0.17 0.17 1.40 83 2.36 1.16 84 1.4 113 0.058 101 102 1.4 -0.8 785 373 411 444 425 487.6 N/A 412 79 79 80 80 74 -0.056 8.02 0.05

60 10.072 10.007 0.17 0.17 1.40 84 2.36 1.16 85 1.4 102 0.066 94 94 1.1 -0.3 687 374 427 450 422 472.0 N/A 360 78 78 79 79 72 -0.051 7.14 0.42

70 11.784 11.676 0.17 0.17 1.43 84 2.29 1.16 86 1.4 98 0.065 96 95 0.9 -0.2 619 381 423 429 412 452.8 N/A 334 77 77 78 78 73 -0.047 6.63 0.58

80 13.487 13.348 0.17 0.17 1.43 85 2.29 1.17 86 1.4 96 0.061 98 98 0.7 -0.2 573 390 403 409 407 436.4 N/A 323 76 76 76 76 72 -0.044 6.57 0.68

90 15.192 15.022 0.17 0.17 1.44 85 2.29 1.16 86 1.4 93 0.054 104 104 0.4 -0.3 544 397 391 393 398 424.6 N/A 313 75 75 75 75 71 -0.045 6.65 0.7

100 16.899 16.696 0.17 0.17 1.44 84 2.28 1.17 86 1.4 93 0.060 99 99 0.2 -0.2 522 404 383 377 393 415.8 N/A 303 75 75 75 75 71 -0.042 6.49 0.77

110 18.606 18.369 0.17 0.17 1.44 84 2.29 1.17 85 1.4 92 0.056 103 102 0.0 -0.2 506 415 380 373 390 412.8 N/A 297 74 74 74 74 71 -0.041 6.1 0.89

Avg/Tot 18.606 18.369 0.17 0.17 1.34 81 1.08 83 107 0.060 100 100 42.0 76 77 77 72 -0.055

Manufacturer:

Model:


Project No.:

Test Date:


Velocity Traverse DataExport to


321

Small Sig

321

Rectangle


Manufacturer: RAIS

Model: Viva L


Tracking No.: 2233

Run: 8

Test Date:
















Complete Test Run









02/13/17






OK

OK

OK


OK



Leakage Rate




OK

321

Small Sig


Model: Viva L

Date: 02/13/17

Run: 8


Test Duration: 110

Output Category: III

HHV Basis LHV Basis






Input (kJ/h) 33,609 31,882 (Btu/h)


MC wet (%) 17.41

MC dry (%) 21.07


CO (g) 199





g/h N/A 108.79



VERSION: 2.2 12/14/2009



321

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Denmark


Section 4

Quality Assurance/Quality Control




Denmark


QUALITY ASSURANCE/QUALITY CONTROL

OMNI follows the guidelines of ISO/IEC 17025, “General Requirements for the Competence of

Testing and Calibration Laboratories,” and the quality assurance/quality control (QA/QC)

procedures found in OMNI’s Quality Assurance Manual.

OMNI’s scope of accreditation includes, but is not limited to, the following:

• ANSI (American National Standards Institute) for certification of product to safety

standards.

• To perform product safety testing by the International Accreditation Service, Inc.

(formerly ICBO ES) under accreditation as a testing laboratory designated TL-130.

• To perform product safety testing as a “Certification Organization” by the Standards

Council of Canada (SCC).

• Serving as a testing laboratory for the certification of wood heaters by the U.S.

Environmental Protection Agency.

This report is issued within the scope of OMNI’s accreditation. Accreditation certificates are

available upon request.

The manufacturing facilities and quality control system for the production of the Viva L Series at

RAIS A/S were evaluated to determine if sufficient to maintain conformance with OMNI’s

requirements for product certification. OMNI has concluded that the manufacturing facilities,

processes, and quality control system are adequate to produce the appliance congruous with the

standards and model codes to which it was evaluated.

This report shall not be reproduced, except in full, without the written approval of OMNI-Test

Laboratories, Inc.




Denmark


Sample Analysis Analysis Worksheets

Tared Filter, Probe, and O-Ring Data


Wood Heater Lab Data - ASTM E2780 / ASTM E2515

Manufacturer: RAIS Equipment Numbers:

Model: Viva L

Tracking No.: 2233


Run #: 1

Date: 2/6/17

TRAIN 1 (First Hour emissions)

Sample Component Reagent Filter, Probe Weights

or Dish # Final, mg Tare, mg Particulate, mg

B. Front filter catch Filter D21 158.8 121.6 37.2

C. Rear filter catch Filter 0.0

D. Probe catch* Probe 0.0 0

E. Filter seals catch* Seals 0.0

Sub-Total Total Particulate, mg: 37.2

TRAIN 1 (Post First Hour Change-out)




C. Rear filter catch Filter D23 121.4 120.7 0.7

D. Probe catch* Probe 16 114269.9 114269.1 0.8 0.12698413

E. Filter seals catch* Seals R417 3293.9 3293.3 0.6


Train 1 Aggregate Total Particulate, mg: 43.5

TRAIN 2



A. Front filter catch Filter D24 164.1 121.7 42.4

B. Rear filter catch Filter D25 123.8 122.9 0.9

C. Probe catch* Probe 17 114563.3 114562.9 0.4 0.00907029

D. Filter seals catch* Seals R418 3324.4 3324.0 0.4

Total Particulate, mg: 44.1

AMBIENT

Sample Component Reagent Filter # or Weights

Probe # Final, mg Tare, mg Particulate, mg

A. Front filter catch* Filter 0.0


Component Equations:

A. Front filter catch Final (mg) - Tare (mg) = Particulate, mg

B. Rear filter catch Final (mg) - Tare (mg) = Particulate, mg

C. Probe catch Final (mg) - Tare (mg) = Particulate, mg


*Particulate catch that results in a negative number, is assumed to be zero for probes

and seals, negative numbers for filters are assumed to be part of the seal weight.


321

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Model: Viva L

Tracking No.: 2233


Run #: 2

Date: 2/7/17


















TRAIN 2








AMBIENT













321

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Model: Viva L

Tracking No.: 2233


Run #: 3

Date: 2/8/17


















TRAIN 2




B. Rear filter catch Filter D35 120.0 120.6 -0.6




AMBIENT













321

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Model: Viva L

Tracking No.: 2233


Run #: 4

Date: 2/9/17













C. Rear filter catch Filter D38 120.8 120.9 -0.1





TRAIN 2








AMBIENT













321

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Model: Viva L

Tracking No.: 2233


Run #: 5

Date: 2/9/17


















TRAIN 2








AMBIENT













321

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Model: Viva L

Tracking No.: 2233


Run #: 6

Date: 2/10/17














D. Probe catch* Probe 66 118461.1 118461.1 0.0 0




TRAIN 2








AMBIENT













321

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Model: Viva L

Tracking No.: 2233


Run #: 7

Date: 2/10/17













C. Rear filter catch Filter D87 123.1 123.2 -0.1





TRAIN 2




B. Rear filter catch Filter D89 120.6 120.9 -0.3




AMBIENT













321

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Model: Viva L

Tracking No.: 2233


Run #: 8

Date: 2/13/17


















TRAIN 2








AMBIENT













321

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Denmark


Calibrations

Methods EPA 28R, ASTM E2515, ASTM E2780

ID # Lab Name/Purpose Log Name Attachment Type

23 Scale-Analytical

Balance Mettler Analytical Balance Calibration Certificate

132 10 lb Weight Weight Standard, 10 lb. Calibration Certificate

185 Platform Scale Weigh-Tronix Platform Scale Calibration Certificate

209 Barometer Barometer – Princo Equipment Record

283A Calibration Weights Troemner Metric Weight Standards Calibration Certificate

296-T55 Tape Measure DeWalt 16’ Tape Measure Calibration Log

335 Sample Box / Dry Gas

Meter Apex Automated Emissions

Sampling Box Calibration Log

336 Sample Box / Dry Gas

Meter Apex Automated Emissions

Sampling Box Calibration Log

340 Wood Moisture Meter Moisture Meter - Delmhorst See Test Run Notes

410 Microtector Dwyer Microtector Calibration Certificate

431 Moisture Meter

Calibrator Delmhorst Moisture Content

Calibrator Calibration Log

559 Vaneometer Dwyer Vaneometer Equipment Record

592 Thermohygrometer Omega Digital Thermohygrometer Calibration Log

594 Combustion Gas

Analyzer ZRE Combustion Gas Analyzer Equipment Record

JJ Calibrations, Inc.7007 SE Lake RdPortland, OR 97267-2105Phone 503.786.3005FAX 503.786.2994

Certificate of CalibrationCertificate Number: 632003

PO:

Property #:

Serial #:

User:

Model:

Description:

Make:

Accuracy:

*Recommended Due:

As Received:

As Returned:

Action Taken:

Order Date:

Procedure:

Calibrated on:

Technician:

°C % RHEnvironment:Department:

E17657

N/A

Mettler

03/27/2017

Within Tolerance

09/27/2016

20

123Adjusted

±0.0004g ±1 LSDDCN 500818/500887

N/A

16010409/27/2016

OMNI-00023

Scale, 205g

Out of Tolerance44

OnSi te

AE200

Authorized By: N/A

0723.01

723A Rice Lake 1mg-200g (Class 0) Mass Set 12/01/2016 603626Std ID Manufacturer Model Nomenclature Due Date Trace ID

Standards Used

ParameterUnit UUT UncertaintyMeasurement Description Range

Measurement Data

Before Accredited = üMin MaxReference *ErrorForce

g 5.7E-04 0.00100 0.0010 0.0000 ü 0.0005 0.0015 g

g 5.7E-04 0.01000 0.0100 0.0000 ü 0.0095 0.0105 g

g 5.7E-04 0.10000 0.1000 0.0000 ü 0.0995 0.1005 g

g 5.7E-04 0.50000 0.5000 0.0000 ü 0.4995 0.5005 g

g 5.7E-04 1.00000 1.0000 0.0000 ü 0.9995 1.0005 g

g 5.7E-04 40.00000 40.0005 0.0005 ü 39.9995 40.0005 g

g 5.7E-04 80.00000 80.0005 0.0005 ü 79.9995 80.0005 g

g 5.7E-04 120.00000 120.0008 0.0008 ü 119.9995 120.0005 g

g 5.8E-04 160.00000 160.0010 0.0010 ü 159.9995 160.0005 g

g 5.7E-04 200.00000 200.0012 0.0012 ü 199.9995 200.0005 g

After Accredited = üMin MaxReference *Error

g 5.7E-04 0.00100 0.0010 0.0000 ü 0.0005 0.0015 g

g 5.7E-04 0.01000 0.0100 0.0000 ü 0.0095 0.0105 g

g 5.7E-04 0.10000 0.1000 0.0000 ü 0.0995 0.1005 g

g 5.7E-04 0.50000 0.5000 0.0000 ü 0.4995 0.5005 g

g 5.7E-04 1.00000 1.0000 0.0000 ü 0.9995 1.0005 g

g 5.7E-04 40.00000 40.0001 0.0001 ü 39.9995 40.0005 g

g 5.7E-04 80.00000 80.0002 0.0002 ü 79.9995 80.0005 g

g 5.7E-04 120.00000 120.0002 0.0002 ü 119.9995 120.0005 g

g 5.8E-04 160.00000 160.0003 0.0003 ü 159.9995 160.0005 g

g 5.7E-04 200.00000 200.0003 0.0003 ü 199.9995 200.0005 g

Remarks: * Many factors may cause the unit to drift out of calibration before the recommended due date. Any reported error is the absolute value between the reference and the unit.

Omni-Test Laboratories13327 NE Airport WayPortland, OR 97230

Calibration

Uncertainties include the effects of the unit.

*

*

Page 1 of 2Certificate: 632003

InspectorRev #Issued 1510/04/2016Reviewer 3

JJ Calibrations, Inc. certifies that this instrument has been calibrated in accordance with the JJ Calibrations Quality Assurance Manual with the stated procedure usingstandards that are traceable to the National Institute of Standards and Technology (NIST), or other National Measurement Institutes (NMI's), or by using naturalphysical constants, intrinsic standards or ratio calibration techniques. The quality system and this certificate are in compliance with ANSI/NCSL Z540-1-1994,ISO/IEC 17025-2005, ISO 10012-1, the ISO 9000 family and QS 9000. The expanded uncertainties of measurements for this calibration are based upon 95%

(2 sigma) confidence limits. Unless otherwise stated, a test accuracy ratio (TAR) of 4:1, if achievable, is maintained. The results reported herein apply only to thecalibration of the item described above. This report may not be reproduced, except in full, without prior written consent of JJ Calibrations, Inc.

JJ Calibrations, Inc. quality system has been assessed and accredited to ISO/IEC 17025:2005.

Page 2 of 2Certificate: 632003

OMNI-Test Laboratories, Inc. Beaverton, OR (503) 643-3788

Control No. M-SFH-0004 (Equipment Record Data Sheet).doc, Effective date: 10/03/2000 Page 1 of 1

Equipment Record Name: Fortin Type Mercurial Barometer

Type of Equipment: Barometer

S/N: 0674 OMNI ID #: OMNI-00209

Manufacturer: PRINCO Instruments, Inc.

Is Manufacturer’s manual available in the equipment file? Yes, if not why?

Date Received: June 2000 Date Placed in Service: June 2000

Condition When Received: New Used Reconditioned

Location: Lab

Location of Calibration Procedures: All PRINCO Fortin mercurial barometers have scales which are set at the time of manufacture to a near zero correction by comparison with a Fortin type mercurial barometer whose scales were calibrated traceable to NIST. If the barometer is not abused an any way , it should never go out of calibration.

Location of Dates/Results of Calibrations: If the barometer is not abused an any way , it should never go out of calibration. The barometer currently hangs on the wall and is never moved.

Location of Maintenance Procedures: Maintenance is performed on an “as needed” basis.

Dates / Results of Maintenance: Regularly scheduled maintenance is not required. Pre-service and post-service maintenance is conducted per QA Manual Section 5.3.5. To date, maintenance has not been required beyond the in-service maintenance prescribed in QA Manual Section 5.3.5.

Any Planned Maintenance? No, if yes what:

Equipment History of any damage, malfunction, modification and/or repair (including a statement on the suitability of the equipment for testing): To date, this instrument has not been damaged, has not malfunctioned, has not been modified, and has not been repaired.

Hearth & Home Technologies Model: Harman Accentra 52i-TC Project: 0135PN031E.REV001

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Thermal Metering System Calibration

Y Factor

Previous Calibration Comparision

Manufacturer: APEX Date 7/7/2016

Acceptable

Deviation (5%) Deviation

Model: XC-60-EP y Factor 0.999 0.04995 0.015

Serial Number: 606001 Acceptance Acceptable

OMNI Tracking No.: OMNI-00335

Calibrated Orifice: FALSE Current Calibration

Acceptable y Deviation 0.020

Average Gas Meter y

Factor

Orifice

Meter

dH@ Maximum y Deviation 0.006 TRUE

0.984 N/A Acceptable dH@ Deviation N/A

Calibration Date: 01/03/17 Maximum dH@ Deviation N/A N/A

Calibrated by: B. Davis Acceptance Acceptable

Calibration Frequency: Six months

Next Calibration Due: 7/3/2017

Instrument Range: 1.000 cfm

Standard Temp.: 68 oF Reference Standard *

Standard Press.: 29.92 "Hg Standard Model Standard Test Meter

Barometric Press., Pb: 30.24 "Hg Calibrator S/N OMNI-00001

Signature/Date: Calib. Date 27-Oct-16

Calib. Value 0.9823 y factor (ref)

Calibration Parameters Run 1 Run 2 Run 3

Reference Meter Pressure ("H2O), Pr 0.00 0.00 0.00

DGM Pressure ("H2O), Pd 2.25 1.25 0.75

Initial Reference Meter 222.4 233.7 238.8

Final Reference Meter 233.608 238.735 244.617

Initial DGM 0 0 0

Final DGM 11.284 5.124 5.938

Temp. Ref. Meter (°F), Tr 67.0 67.0 68.0

Temperature DGM (°F), Td 78.0 78.0 79.0

Time (min) 53.0 32.0 48.0

Net Volume Ref. Meter, Vr 11.208 5.035 5.817

Net Volume DGM, Vd 11.284 5.124 5.938

Gas Meter y Factor = 0.991 0.982 0.981

Gas Meter y Factor Deviation (from avg.) 0.006 0.002 0.004

Orifice dH@ N/A N/A N/A

Orifice dH@ Deviation (from avg.) N/A N/A N/A

where:

1. Deviation = |Average value for all runs - current run value|

** 2. y = [Vr x (y factor (ref)) x (Pb + (Pr/ 13.6)) x (Td + 460) ]/ [Vd x (Pb + (Pd / 13.6)) x (Tr + 460)]

** 3. dH@ = 0.0317 x Pd / (Pb (Td + 460)) x [ (Tr + 460) x time) / Vr ]^2

* Reference calibration is traceable to NIST through NIST Test # 40674, Kimble ASTM E1272, or NIST traceable laboratory

** Equations come from EPA Method 5

The uncertainty of measurement is ±0.14 ft3/min. This is based on the reference standard having a TAR (Test Accuracy Ratio) of at least 4:1.

Yes

Control No. C-SSB-0005, Effective Date: 7/7/2011


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1/6/2017


Control No. C-SFAK-0001, Effective date: 12/2/2015 Page 1 of 1

DIFFERENTIAL PRESSURE GAUGE CALIBRATION DATA SHEET

Instrument to be calibrated: __Pressure Transducer_____________ Maximum Range: 2” W.C. ID Number: OMNI-00335B Calibration Instrument: Digital Manometer ID Number: OMNI-00633 Date: 1/3/17 By: B. Davis This form is to be used only in conjunction with Standard Procedure C-SPC.

*Acceptable tolerance is 4%. The uncertainty of measurement is ±0.4” WC. This is based on the reference standard having a TAR (Test Accuracy Ratio) of at least 4:1.

Technician signature: Date: 1/3/17 Reviewed by: Date:

Range of Calibration Point

(″WC)

Digital Manometer

Input (″WC)

Pressure Gauge Response

(″WC)

Difference (Input -

Response)

% Error of Full Span*

0-20% Max. Range 0 – 0.4

0.155 0.16 0.005 0.25

20-40% Max. Range 0.4 – 0.8

0.505 0.50 0.005 0.25

40-60% Max. Range 0.8 – 1.2

1.001 1.00 0.001 0.05

60-80% Max. Range 1.2 – 1.6

1.495 1.48 0.015 0.75

80-100% Max. Range 1.6 – 2.0

1.985 1.99 0.005 0.25


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Thermal Metering System Calibration

Y Factor

Previous Calibration Comparision

Manufacturer: APEX Date 7/7/2016

Acceptable

Deviation (5%) Deviation

Model: XC-60-EP y Factor 1.005 0.05025 0.015

Serial Number: 606002 Acceptance Acceptable

OMNI Tracking No.: OMNI-00336

Calibrated Orifice: FALSE Current Calibration

Acceptable y Deviation 0.020

Average Gas Meter y

Factor

Orifice

Meter

dH@ Maximum y Deviation 0.002 TRUE

0.990 N/A Acceptable dH@ Deviation N/A

Calibration Date: 01/03/17 Maximum dH@ Deviation N/A N/A

Calibrated by: B. Davis Acceptance Acceptable

Calibration Frequency: Six months

Next Calibration Due: 7/3/2017

Instrument Range: 1.000 cfm

Standard Temp.: 68 oF Reference Standard *

Standard Press.: 29.92 "Hg Standard Model Standard Test Meter

Barometric Press., Pb: 30.24 "Hg Calibrator S/N OMNI-00001

Signature/Date: Calib. Date 27-Oct-16

Calib. Value 0.9823 y factor (ref)

Calibration Parameters Run 1 Run 2 Run 3

Reference Meter Pressure ("H2O), Pr 0.00 0.00 0.00

DGM Pressure ("H2O), Pd 1.90 1.00 0.70

Initial Reference Meter 249.7 257 262.227

Final Reference Meter 256.938 262.17 269.982

Initial DGM 0 0 0

Final DGM 7.263 5.214 7.847

Temp. Ref. Meter (°F), Tr 68.0 68.0 68.0

Temperature DGM (°F), Td 76.0 79.0 79.0

Time (min) 34.0 33.0 59.0

Net Volume Ref. Meter, Vr 7.238 5.170 7.755

Net Volume DGM, Vd 7.263 5.214 7.847

Gas Meter y Factor = 0.989 0.992 0.989

Gas Meter y Factor Deviation (from avg.) 0.001 0.002 0.001

Orifice dH@ N/A N/A N/A

Orifice dH@ Deviation (from avg.) N/A N/A N/A

where:

1. Deviation = |Average value for all runs - current run value|

** 2. y = [Vr x (y factor (ref)) x (Pb + (Pr/ 13.6)) x (Td + 460) ]/ [Vd x (Pb + (Pd / 13.6)) x (Tr + 460)]

** 3. dH@ = 0.0317 x Pd / (Pb (Td + 460)) x [ (Tr + 460) x time) / Vr ]^2

* Reference calibration is traceable to NIST through NIST Test # 40674, Kimble ASTM E1272, or NIST traceable laboratory

** Equations come from EPA Method 5

The uncertainty of measurement is ±0.14 ft3/min. This is based on the reference standard having a TAR (Test Accuracy Ratio) of at least 4:1.

Yes

Control No. C-SSB-0005, Effective Date: 7/7/2011


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Control No. C-SFAK-0001, Effective date: 12/2/2015 Page 1 of 1

DIFFERENTIAL PRESSURE GAUGE CALIBRATION DATA SHEET

Instrument to be calibrated: __Pressure Transducer_____________ Maximum Range: 2” W.C. ID Number: OMNI-00336B Calibration Instrument: Digital Manometer ID Number: OMNI-00633 Date: 1/3/17 By: B. Davis This form is to be used only in conjunction with Standard Procedure C-SPC.

*Acceptable tolerance is 4%. The uncertainty of measurement is ±0.4” WC. This is based on the reference standard having a TAR (Test Accuracy Ratio) of at least 4:1.

Technician signature: Date: 1/3/17 Reviewed by: Date:

Range of Calibration Point

(″WC)

Digital Manometer

Input (″WC)

Pressure Gauge Response

(″WC)

Difference (Input -

Response)

% Error of Full Span*

0-20% Max. Range 0 – 0.4

0.134 0.140 0.006 0.30

20-40% Max. Range 0.4 – 0.8

0.514 0.52 0.006 0.30

40-60% Max. Range 0.8 – 1.2

0.925 0.93 0.005 0.25

60-80% Max. Range 1.2 – 1.6

1.356 1.35 0.006 0.30

80-100% Max. Range 1.6 – 2.0

1.917 1.91 0.007 0.35


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YES X NO

1) Complete Calibration documentation

Vaneometer, Air Vel. Meter - Dwyer

OMNI-00559

New vane installed

480

(Check 'X' for answer)

Cab 1

Active

T36Z

5/15/2017

11/15/2016

6

6 month

OMNI in house

Reference Standard:

Location of Equipment:

Do the following:

Date of Next Calibration

Date of Last Calibration

Calibration Period (Months)

Type of Calibration

Calibration Vendor

Part #

OMNI Track #

Equipment Name/Description

Equipment S/N:

Comments

Status


2) Complete top half of this form

3) Attach appropriate calibration forms and save in following location

\\omni-serv\Test Equipment\Equipment\OMNI-XXXXX - Equipment Name

4) Repopulate database with updated information

5) Print, laminate and adhere calibration tag to equipment

Do the following:

Six MonthOMNI-00559Vaneometer

Last Cal Date: 11/15/2016Due Date of Cal: 5/15/2017

Six MonthOMNI-00559Vaneometer

Last Cal Date: 11/15/2016Due Date of Cal: 5/15/2017


39 of 143


40 of 143

YES X NO


Part #

OMNI Track #

Equipment Name/Description

Equipment S/N:

Comments

Status

Reference Standard:

Location of Equipment:

Do the following:

Date of Next Calibration

Date of Last Calibration

Calibration Period (Months)

Type of Calibration

Calibration Vendor

Portable gas cart.

Active, calibrate prior to use.

N5F0112

N/A

N/A

N/A

Calibrate Prior to use.

OMNI in house

CAI ZRE-4 Gas Analyzer

OMNI-00594

CO2, O2, and dual range CO gas analyzer.

ZRE-4

(Check 'X' for answer)


2) Complete top half of this form

3) Attach appropriate calibration forms and save in following location

\\omni-serv\Test Equipment\Equipment\OMNI-XXXXX - Equipment Name

4) Repopulate database with updated information

5) Print, laminate and adhere calibration tag to equipment

Do the following:

Verify before useOMNI-00594Gas Analyzer

Verify before useOMNI-00594Gas Analyzer




Denmark


Example Calculations


Equations and Sample Calculations – ASTM E2780 & E2515

Manufacturer:

Model:

Run:

Category:

MSdb – Weight of test fuel spacers, dry basis, kg

MCdb– Weight of test fuel crib, excluding nails and spacers, dry basis, kg

DCdb - Density of fuel crib, excluding spacers and nails, dry basis, lbs/ft3

MFTAdb - Total weight of fuel crib excluding nails, dry basis, kg

BR – Dry burn rate, kg/hr

Vs – Average gas velocity in the dilution tunnel, ft/sec

Qsd – Average gas flow rate in dilution tunnel, dscf/hr

Vm(std) – Volume of gas sampled, corrected to dry standard conditions, dscf

mn – Total particulate matter collected, mg

Cs - Concentration of particulate matter in tunnel gas, dry basis, corrected to standard conditions, g/dscf

ET – Total particulate emissions, g

PR - Proportional rate variation

PMR – Particulate emissions for test run, g/hr

PMF – Particulate emission factor for test run, g/dry kg of fuel burned

RAIS

Viva L

1

II

are provided for each equation. The raw data and printout results from a sample run are also provided for

Equations used to calculate the parameters listed below are described in this appendix. Sample calculations

comparison to the sample calculations.



MSdb – Weight of test fuel spacers, dry basis, kg

ASTM E2780 equation (1)

MSdb = (MSwb )(100/(100 + FMS))

Where,

FMS = average fuel moisture of test fuel spacers, % dry basis

MSwb = weight of test fuel spacers, wet basis, kg

Sample Calculation:

FMS = 20.9 %

MSwb = 2.0 lbs

0.4536 = Conversion factor from lbs to kg

MSdb = [( 2.0 x 0.4536) (100/(100 + 20.9 )

MSdb = 0.8 kg



MCdb– Weight of test fuel crib, excluding nails and spacers, dry basis, kg


MCdb = Σ[(MCPnwb)(100/(100 + FMCPn))]

Where,

MCPnwb = weight of each test fuel piece n in fuel crib, excluding nails and spacers, wet basis, kg

FMCPn = Average fuel moisture of test fuel n in fuel crib, % dry basis

Sample Calculation (test fuel piece 1):

MCPnwb = 1

FMCPn = 22.9

= 1.0 (100/(100+ 22.9 )

= 0.8 lbs

Total crib weight, excluding spacers =5.22 lbs

MCdb = 2.37 kg



DCdb - Density of fuel crib, excluding spacers and nails, dry basis, lbs/ft3


DCdb = MCdb/VC

Where,

VC = Volume of fuel crib, ft3

Sample calculation:

VC = 307 in3

1728 = conversion from in3 to ft

3

DCdb = 5.22 / 307 * 1728

= 29.4 lbs/ft3



MFTAdb - Total weight of fuel crib excluding nails, dry basis, kg


MFTAdb = MSdb + MCdb

Sample calculation:

MFTAdb = 0.75 + 2.37

= 3.12 kg



BR – dry burn rate, kg/hr


60 MFTAdb

θ

Where,

θ = Total length of test run, min

Sample Calculation:

MBdb = 3.12 kg

θ = 180 min

60 x 3.12

BR = 1.04 kg/hr

BR =

BR = 180



Vs – Average gas velocity in the dilution tunnel, ft/sec

ASTM E2515 equations (9)

Where:

vscent = Dilution tunnel velocity calculated after the multi-point pitot traverse at the center, ft/sec

vstrav = Dilution tunnel velocity calculated after the multi-point pitot traverse, ft/sec

kp = Pitot tube constant, 85.49

Cp = Pitot tube coefficient: 0.99, unitless

ΔP* = Velocity pressure in the dilution tunnel, in H2O

Ts = Absolute average gas temperature in the dilution tunnel, °R; (°R = °F + 460)

Ps = Absolute average gas static pressure in dilution tunnel, = Pbar + Pg , in Hg

Pbar = Barometric pressure at test site, in. Hg

Pg = Static pressure of tunnel, in. H20; (in Hg = in H20/13.6)

Ms = **The dilution tunnel wet molecular weight; Ms = 28.78 assuming a dry weight of 29 lb/lb-mole

Sample calculation:

17.78

20.18

85.6 + 1/2

Vs = 0.881 x 85.49 x 0.99 x 0.297 x -0.28

13.6

Vs = 17.67 ft/s

*The ASTM test standard mistakenly has the square root of the average delta p instead of

the average of the square root of delta p. The current EPA Method 2 is also incorrect. This

was verified by Mike Toney at EPA.

**The ASTM test standard mistakenly identifies Ms as the dry molecular weight. It should be

the wet molecular weight as indicated in EPA Method 2.

28.7829.75 +((

Fp = = 0.881

)460

) x

, ASTM E2515 Equation (1)Fp = Adjustment factor for center of tunnel pitot tube placement, Fp = Vstrav

Vscent

ss

avgs

avgppPsMP

TPCkFv

)()(



Qsd – Average gas flow rate in dilution tunnel, dscf/hr


Where:

3600 = Conversion from seconds to hours (ASTM method uses 60 to convert in minutes)

Bws = Water vapor in gas stream, proportion by volume; assume 2%

A = Cross sectional area of dilution tunnel, ft2

Tstd = Standard absolute temperature, 528 °R

Ps = Absolute average gas static pressure in dilution tunnel, = Pbar + Pg , in Hg

Ts(avg) = Absolute average gas temperature in the dilution tunnel, °R; (°R = °F + 460)

Pstd = Standard absolute pressure, 29.92 in Hg

Sample calculation: -0.28

13.6

85.6 + 460

Qsd = ##### dscf/hr

29.9217.67 x 0.196 x

528x

29.8 +

Qsd = 3600 x (1 - 0.02) x

std

s

avgs

stdswssd

P

P

T

TAvBQ

)(

)1(3600



Vm(std) – Volume of Gas Sampled Corrected to Dry Standard Conditions, dscf


Where:

K1 = 17.64 °R/in. Hg

Vm = Volume of gas sample measured at the dry gas meter, dcf

Y = Dry gas meter calibration factor, dimensionless

Pbar = Barometric pressure at the testing site, in. Hg

∆H = Average pressure differential across the orifice meter, in. H2O

Tm = Absolute average dry gas meter temperature, °R

Sample Calculation:

Using equation for Train 1: 1.31

Vm(std) = 17.64 x 29.793 x 0.984 x 13.6

( 80.7 + 460 )

Vm(std) = 28.550 dscf

Using equation for Train 2: 1.16

Vm(std) = 17.64 x 30.524 x 0.99 x 13.6

( 80.8 + 460 )

Vm(std) = 29.409 dscf

Using equation for ambient train: 0.00

Vm(std) = 17.64 x 0.00 x 1 x 13.6

( 70.4 + 460 )

Vm(std) = 0 dscf

(

( 29.75 + )

( 29.75 )+

29.75 + )



mn – Total Particulate Matter Collected, mg

ASTM E2515 Equation (12)

Where:

mp = mass of particulate matter from probe, mg

mf = mass of particulate matter from filters, mg

mg = mass of particulate matter from filter seals, mg

Sample Calculation:

Using equation for Train 1 (first hour):

mn = 0.0 + 37.2 + 0.0

mn = 37.2 mg

Using equation for Train 1 (post-first hour):

mn = 0.8 + 4.9 + 0.6

mn = 6.3 mg

Train 1 aggregate:

mn = 37.2 + 6.3

mn = 43.5 mg

Using equation for Train 2:

mn = 0.4 + 43.3 + 0.4

mn = 44.1 mg

gfpn mmmm



Cs - Concentration of particulate matter in tunnel gas, dry basis, corrected to standard conditions, g/dscf


Where:

K2 = Constant, 0.001 g/mg

mn = Total mass of particulate matter collected in the sampling train, mg

Vm(std) = Volume of gas sampled corrected to dry standard conditions, dscf

Sample calculation:

For Train 1:

43.5

28.55

Cs = 0.00152 g/dscf

For Train 2

44.1

29.41

Cs = 0.00150 g/dscf

For Ambient Train

0.0

0

Cr = 0 g/dscf

0.001 x

Cs = 0.001 x

Cr = 0.001 x

Cs =

)(

2

stdm

ns

V

mKC



ET – Total Particulate Emissions, g


Where:

Cs = Concentration of particulate matter in tunnel gas, g/dscf

Cr = Concentration particulate matter room air, g/dscf

Qstd = Average dilution tunnel gas flow rate, dscf/hr

θ = Total time of test run, minutes

Sample calculation:

For Train 1

ET = ( 0.001524 - 0 ) x ###### x 180 /60

ET = 53.79 g

For Train 2

ET = ( 0.001500 - 0 ) x ###### x 180 /60

ET = 52.94 g

Average

E = 53.37 g

Total emission values shall not differ by more than 7.5% from the total average emissions

7.5% of the average = 4.00

Train 1 difference = 0.43

Train 2 difference = 0.43

stdrsT QccE



PR - Proportional Rate Variation


Where:

θ = Total sampling time, min

θi = Length of recording interval, min

Vmi = Volume of gas sample measured by the dry gas meter during the “ith”

time interval, dcf

Vm = Volume of gas sample as measured by dry gas meter, dcf

Vsi = Average gas velocity in the dilution tunnel during the "ith" time interval, ft/sec

Vs = Average gas velocity in the dilution tunnel, ft/sec

Tmi = Absolute average dry gas meter temperature during the "ith" time interval, oR

Tm = Absolute average dry gas meter temperature, oR

Tsi = Absolute average gas temperature in the dilution tunnel during the "ith" time interval, oR

Ts = Absolute average gas temperature in the dilution tunnel, oR

Sample calculation (for the first 1 minute interval of Train 1):

180 x 1.666 x 17.67 x ( 85.0 + 460 ) x ( 80.7 + 460 )

10 x 29.79 x 17.66 x ( 85.6 + 460 ) x ( 74.0 + 460 )

PR = 102 %

x 100)(PR =

100

smisimi

simsmi

TTVV

TTVVPR



PMR – Particulate emissions for test run, g/hr


PMR = 60 (ET/θ)

Where,

ET = Total particulate emissions, grams

θ = Total length of full integrated test run, min

Sample Calculation:

ET (Dual train average) = 53.37 g

θ = 180 min

PMR = 60 x ( 53.37 / 180 )

PMR = 17.79 g/hr



PMF – Particulate emission factor for test run, g/dry kg of fuel burned


PMF = ET/MFTAdb

Sample Calculation:

ET (Dual train average) = 53.37 g

MBdb = 3.12 kg

PMF = 53.37 / 3.12

PMF = 17.10 g/kg


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